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US5055198A - Autologous blood recovery membrane system and method - Google Patents

Autologous blood recovery membrane system and method
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US5055198A
US5055198AUS07/525,536US52553690AUS5055198AUS 5055198 AUS5055198 AUS 5055198AUS 52553690 AUS52553690 AUS 52553690AUS 5055198 AUS5055198 AUS 5055198A
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blood
filter
conduit
washing fluid
vacuum
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US07/525,536
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U. Ramakrishna Shettigar
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Asahi Kasei Medical Co Ltd
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Priority to EP91906022Aprioritypatent/EP0518975B1/en
Priority to JP3506174Aprioritypatent/JP3012689B2/en
Priority to PCT/US1991/001530prioritypatent/WO1991013677A1/en
Priority to US07/730,705prioritypatent/US5215519A/en
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Assigned to ASAHI MEDICAL CO; LTD.reassignmentASAHI MEDICAL CO; LTD.ASSIGNMENT OF ASSIGNORS INTEREST.Assignors: SHETTIGAR, UDIPI R.
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Abstract

An apparatus for recycling autologous blood from a patient for reinfusion back to the patient comprising suction means, admixing means for admixing aspirated blood with a washing fluid, filtering means for filtering the admixture through an emboli filter and a membrane filter, monitoring means for measuring the amount of cellular component volume in the filtered blood, filtration means for removing excess fluid and particulates from the blood, and reinfusion means is disclosed. Embodiments for use during surgery for on-line purification and reinfusion on a real time basis are disclosed along with embodiments for use post-surgically when the wound site is closed and drainage tubing has been implanted at the wound site to draw off blood post-surgically. Methods for performing the autotransfusion process are also disclosed.

Description

RELATED APPLICATION
This application is a continuation-in-part of applicant's copending application Ser. No. 491,183 filed Mar. 7, 1990, now abandoned, the contents of which are incorporated by this reference.
BACKGROUND
1. Field of the Invention
The present invention pertains to methods and apparatus for recovery, purification and reinfusion of blood lost at a wound site, either during a surgical or postsurgical management period. More specifically, the present invention applies to aspiration of shed blood from a wound site during intraoperative or postsurgical recovery periods, on-line purification of aspirated blood by filtration and cell-washing using membranes, and reinfusion of purified autologous blood to the patient on a real time basis. With some modifications, the present invention may be used as a hemofiltration or ultrafiltration system for the treatment of acute and end-stage renal diseases.
2. Statement of the Art
Significant blood loss to a person may occur during a traumatic injury, such as an auto accident, or during a serious and traumatic surgery, such as open heart surgery, or during a postsurgical recovery period due to hemorrhagic conditions. Significant loss in blood results in decreased blood pressure, decreased cardiac output, and decreased oxygen delivery to tissues, particularly brain cells. For these reasons, it is necessary to compensate the loss in blood by transfusing the patient with blood as soon as possible.
During an intraoperative period, a pool of shed blood accumulates in the wound site which obstructs the surgery site unless it is aspirated out therefrom. Usually, suction is provided to remove the shed blood, other accumulated fluids, blood clots and other tissue debris. The total loss of blood may vary from 1,000 ml to 15,000 ml depending on the extent of the surgery and the attendant traumatic conditions.
During a postsurgical recovery period due to hemorrhagic conditions, the closed wound may continue to bleed into the chest, pleural cavity, or abdominal cavity. On an average, 1,000 ml of blood is usually lost over a five hour period. However, blood loss could conceivably be as high as 21,350 ml. In such instances, the patient may have to be rushed back to surgery to correct the underlying problem. It is obvious that blood transfusion is imperative under such conditions. Usually, the shed blood is drained from the body cavity using drainage tubing under a controlled suction. The drained blood is generally collected in a container.
Blood shed during intraoperative or postsurgical recovery periods can be collected in a container and reinfused to the patient provided the salvaged blood is free of impurities. Typical impurities are blood clots, tissue debris, hair, foreign particles, activated coagulation factors, denatured proteins, plasma free hemoglobin, and any other fluids (e.g. irrigation fluid) that are being introduced into the wound site by medical personnel.
Impurities in salvaged blood are conventionally filtered out using a 40 micron filter to remove particles greater than 40 microns in size, and the blood is then subjected to "cell washing." The cell washing technique may involve mixing blood with a physiological solution (e.g., saline or Ringer's) in equal proportion to the blood. The blood is then centrifuged to recover the heavier blood cells which are suitable for reinfusion to the patient. The lighter portion of the centrifuged fluid (i.e., the top portion of the centrifuge tube content) containing platelets, white cells, plasma proteins and antibodies is usually discarded as waste. This is a significant loss to the patient, particularly the loss of coagulation factors, platelets, white cells and antibodies. Therefore, the efficiency of recovery of blood products by conventional cell washing techniques is low. Additionally, conventional blood recovery methods are not accomplished on-line, and in real time. Rather, they are batch processes involving operator intervention, and are subject to human errors and time delay.
Thus it will be appreciated that purification of salvaged blood based on cell-centrifuge machines are not designed to work on a real time basis. That is, there is considerable lag time (more than 15 minutes) between the moment of aspiration of blood and reinfusion of processed autologous blood. This is a significant problem, especially when the patient bleeds rapidly, and his/her lost blood volume needs to be compensated immediately. Furthermore, during cell washing by the centrifuge technique, a significant amount of red blood cells are lost, and almost all white blood cells, platelets and plasma proteins including antibodies.
Due to the aforementioned problems in the conventional cell washing technique, a patient is usually given homologous (donor) blood transfusions rather than his/her own blood, which is still being processed.
Problems with homologous blood transfusion are many. The major problem is providing suitable donor blood which will not cause side effects, such as anaphylactic reactions, and which does not contain donor-associated infections, such as hepatitis, malaria, or acquired immune deficiency syndrome (AIDS). At times, it is difficult to find appropriate types and amounts of blood necessary for transfusions, and it can become very expensive.
Due to the aforementioned problems, "autotransfusion" (reuse of a patient's own blood) has received significant attention. A number of autotransfusion systems have been developed in recent years with varying system configurations. They are composed of three basic units; an aspirator unit, a cell washing unit, and a reinfusion unit.
The typical aspirator unit consists of a suction handle attached to suction tubing which is connected to an emboli filter reservoir. The emboli filter is generally provided with an air vent line, a degassifier, a filter, and a blood reservoir. Controlled suction is usually applied with a vacuum source via a vent line. The vacuum aspirates shed blood, along with other impurities, from the wound site. Larger impurities are trapped in the emboli filter.
Filtered blood is usually pumped to a cell centrifuge machine where it is mixed with an appropriate "washing fluid" and centrifuged for a specified time period until the heavier blood cells are separated from the plasma. This method is typically cumbersome, time consuming, and requires an operator to attend to the system continuously. Furthermore, there is a loss of precious plasma proteins, antibodies, and white blood cells which are important for the body's ability to fight infection. Thus, it would be an advancement in the art to provide on-line, continuous methods and apparatus for blood purification which would minimize loss of precious blood elements, and would reinfuse to the patient his/her own blood on a real time basis. It would be a further advancement to provide an automatic system which would reinfuse whole blood at a specified hematocrit level free of air emboli.
The aforementioned prior art systems are designed to be used during surgery (i.e., intraoperative period). During the post-surgical recovery period, bleeding may still continue from the closed wound, but at a significantly reduced flow rate. Bleeding usually progresses at about 1,000 ml over a five hour period. Post-surgical autotransfusion of shed blood is particularly useful in postoperative management of patients with serious hemorrhage. Post-surgical blood losses may range from 2,050 ml to 21,350 ml. The shed blood is usually drained using a drainage unit by a controlled suction.
There are many chest drainage units on the market. Examples are the "Pleur-evac" chest drainage unit by Deknatel, Howmedica, Inc., New York; "Sentinel Seal Compact" "chest drainage unit" by Argyle; "Snyder Hemovac Compact Evacuator", Zimmer Corp., Dover, Ohio; and "Sorenson Autotransfusion System", Salt Lake City, Utah. In all these drainage units, a controlled suction (i.e., where negative pressure does not exceed -25 Cm of water) is applied to drain the shed blood from the closed wound site via one or two drainage tube. The drained blood is filtered to remove solid particulates and is collected in a bag. When a suitable volume of blood is collected, it can be reinfused to the patient directly without washing the blood cells, or it can be reinfused to the patient after it is washed with saline solution using a cell centrifuge machine. A 40 micron filter (e,g., a "Pall filter") is typically used during reinfusion of the blood. Care is taken to protect the closed wound from excessive negative pressure (e.g., greater than -20 Cm water), and to minimize the blood-air interface.
None of the aforementioned systems wash the blood on-line; rather, the washing needs to be done in a batch operation using a cell centrifuge. Since a controlled suction is applied to the drainage tubing using a vacuum pump, the blood-air interface is not completely eliminated in those systems. Thus, it would be an advancement in the art to provide an automatic post-surgical autotransfusion system which eliminates the problems described above.
SUMMARY OF THE INVENTION
The invention is generally directed to the filtration and processing of blood aspirated from a patient, either during or after surgery, for ultimate reinfusion into the patient. The invention generally includes means for aspirating blood from the wound site, means for admixing a washing fluid with the aspirated blood, means for filtering air emboli, particulate matter, unwanted impurities, and excess fluid from the blood, and means for reinfusion of the purified blood into the patient.
Embodiments of the invention are directed to use during a surgical procedure when the wound site is open, and other embodiments of the invention are directed to use during postsurgical recovery for draining blood which may be lost from a closed wound site as a result of hemorrhage conditions.
Blood is aspirated from a wound site by suction means which may typically include a suction tip and handle for directing the tip into the wound site. Suction is accomplished by attachment of a vacuum source to the system which applies a negative pressure of up to -200 mm Hg. Washing fluid, which is retained in a suitable retainer means, is mixed with the aspirated blood. The washing fluid retainer means may be either a collapsible bag, a non-collapsible bag, or a similarly suitable retainer. The washing fluid may be any type of conventional fluid used in surgery, such as normal saline or Ringer's solution, and may contain an appropriate anticoagulant substance, such as heparin. The washing solution, which aids in removal of impurities, is admixed with the aspirated blood in approximate proportion to the amount of blood aspirated.
Washing fluid admixed with aspirated blood aids in purifying the blood of impurities. Therefore, it is desirable that washing fluid be introduced into the aspirated blood in approximately equal proportion thereto. The admixture of equal proportions of blood and washing fluid could be accomplished by use of sophisticated machinery. However, in the interest of simplicity, some embodiments of the invention employ a novel method of attaining equal proportions of blood and washing fluid. The embodiments are configured so that the washing fluid retainer is approximately two feet below the height of the suction means. When blood is aspirated into the system, it causes the negative pressure applied to the system to increase. The increase in negative pressure results in the increase of negative pressure acting upon the washing fluid retainer, and washing fluid is thereby urged into the system in proportion to the amount of blood being aspirated. Conversely, when no blood is being aspirated, the negative pressure created by the vacuum in the suction means is too low to draw any washing fluid into the system. The flow resistance of blood being aspirated into, or conducted through, the system is influenced by the diameter of tubing used. Therefore, the size of tubing used in the system should be from about 4 mm to about 10 mm in diameter.
The present invention provides a continuous on-line method of removing air, impurities, unwanted cellular and blood components, and excess fluid. The blood and washing fluid admixture is directed through an emboli filter which traps and removes air bubbles from the admixture. The emboli filter is also capable of trapping particulate matter of relatively large size. An emboli filter has been especially designed to enhance the separation of particulates and air bubbles from the aspirated blood and washing fluid admixture.
The blood and washing fluid admixture is also directed through a membrane filter, which may be an ultrafilter or a plasma filter, which removes smaller impurities along with excess fluid. The unwanted components and excess fluids which are filtered from the blood is drawn off into filtrate retention means. In some embodiments of the invention, the blood is continuously recirculated through the filtering system until a sufficient amount of fluid has been removed and a specified level of desired blood components (i.e., hematocrit level) has been attained. This is determined by monitoring means associated with the apparatus. Recirculation may be accomplished by mechanical means, such as a roller pump, or may be accomplished manually by, for example, applying alternating force or pressure which may force the admixture to pass through the filter means continuously. When the blood component portion of the blood has reached a specified level, the blood is reinfused into the patient. The specific level of desired blood components, or the hematocrit level, will be determined by the attending medical personnel.
In alternative embodiments, the blood is not recirculated. Rather, the blood is passed through an integrated emboli filter and membrane filter. When sufficient amounts of excess fluid have been removed, as measured by monitoring means, the filtered blood is ready for reinfusion into the patient.
The monitoring means for use in this system may be any means which determines the amount of fluid in the blood being circulated through the system. For example, such a monitor may constantly monitor the fraction of noncellular fluid volume in the blood by measuring the impedance of blood at a specified frequency using two stainless steel electrodes located in proximity to the filter means. Measured conductivity of blood is known to be proportional to the fraction of noncellular fluid volume in the blood. Such conductivity monitors are available on the market (e.g., Sedatelec, Chemin des Muriers, Irigny, France).
In an alternative embodiment of the invention, a further filter, similar to the emboli filter of the system, is associated with the reinfusion system and operates to remove any residual air bubbles before the blood is reinfused.
Membrane filters which can be used in the invention to purify blood are those which have the capability of trapping unwanted impurities of a particular size. For example, an ultrafilter may be used which is a conventional membrane separator having a pore size ranging from about 40,000 daltons to about 400,000 daltons molecular weight cut off. A preferred pore size is about 100,000 daltons. Representative filters are ultrafilters manufactured by the Kuraray Company of Japan. However, if larger impurities are to be removed, a plasma filter having a pore size larger than about 400,000 daltons, and up to 0.4 microns, may be preferred.
Blood which has been filtered, and which comprises appropriate levels of blood cellular components and fluid, is collected in blood collection means. The blood collection means may be a collapsible bag or a rigid, non-collapsible bag. The invention, whether highly mechanized or simplistically configured, is designed to process blood on a real-time basis. The filtered blood may be collected in a bag and reinfused by a batch-type process, or the collected blood may be constantly reinfused from the apparatus of the invention. If collected by batch processing, the filtered blood may be collected in a bag and may be attached, for example, to an I.V. pole for reinfusion. Alternatively, the blood may be infused continuously to the patient from a reinfusion line connected to the blood collection means of the system.
The invention may be configured as a stand-alone unit which can, for example, be wheeled into the operating forum or intensive care unit following surgery. Alternatively, the invention may be configured as a portable system attached to a conventional I.V. pole.
Embodiments of the invention employ varying degrees of mechanization to accomplish the different steps of blood aspiration and filtration. Those systems which are less mechanized are preferred embodiments since they allow easier handling, are less dependent on mechanical and electrical components which may fail, and are ultimately less expensive. One embodiment of the invention, for example, presents a "machineless" means of filtering blood. That is, it uses the force of gravity to accomplish filtration of aspirated blood and washing fluid through the membrane filter, and to drain filtrate (waste). Gravity and manipulation of negative pressure applied to the system effectuates recirculation of the admixed blood and washing fluid through the membrane filter for filtering. Thus, aspiration and filtration of the blood through this, the simplest of embodiments, is accomplished with no collateral machinery other than a vacuum source.
Other embodiments may employ pumps, such as roller pumps, to provide movement to the circulating admixture in the system, and to provide slight pressure at various points. For example, pumps may be used to infuse washing fluid into the system for admixture with the aspirated blood, to aid in drainage of filtrate from the membrane filter, to aid in reinfusion, and to cause recirculation of the blood and washing fluid admixture through the system.
In a more mechanized embodiment, a series of pumps, valves, and blood level detectors may be in electrical or mechanical communication with each other such that processing of the blood is fully automated. In some embodiments, for example, aspirated blood is filtered through an emboli filter and collects temporarily in a reservoir associated with the emboli filter. Blood level detectors connected to the reservoir measure a high level of blood in the reservoir and a low level of blood in the reservoir. The blood level detectors may be ultrasonic bubble detectors which detect the presence of air in the system, thereby signalling when blood level has dropped. A signal is thus communicated to a recirculation pump when the blood level is high in the reservoir, causing the pump to pump faster. Correspondingly, a signal is sent to the recirculation pump when the level of blood gets too low in the reservoir, and the recirculation pump slows or stops.
As the blood/washing fluid admixture circulates through a membrane filter, fluid and other waste components are removed. Removal of the filtrate may be increased by a filtration pump associated with the filtrate drainage means. As the filtered blood exits the membrane filter, a monitor determines the amount of fluid and desired blood components in the blood. If there is an excess of fluid still remaining in the blood, the recirculation continues. However, when the proper amount of fluid has been removed, as determined by the monitor, a signal is sent to a shunting valve which closes off the pathway to recirculation, and opens the pathway to reinfusion. The blood is filtered once more of air bubbles and monitored. If no air bubbles exist, a signal is sent from the detector to a reinfusion valve which then opens, allowing the filtered blood to be reinfused into the patient. The reinfusion valve may also be in communication with the blood level detectors of the reservoir such that if the blood level in the reservoir is too low, the reinfusion valve will not open.
The invention may be used during surgery or post-surgically. Embodiments for postsurgical use provide a method of controlled negative pressure in the drainage tubing, which is implanted in the closed wound site and is used to drain blood from the area. By controlling the negative pressure in the drainage tubing, blood may be aspirated without introduction of air into the system. This has the obvious advantage of reducing air emboli, and it further lessens protein denaturation as a result. Postsurgical embodiments may be mechanized to varying degrees, as discussed above, or may be fairly simple and manually operated. Such embodiments are easy to handle, are less expensive, and are less subject to mechanical failure.
The embodiments of the invention may be more clearly understood from the drawings and description which follow.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is a schematic diagram illustrating an embodiment of the invention which is an intraoperative autotransfusion system;
FIG. 2 is a front view of the embodiment shown in FIG. 1;
FIG. 3 is a schematic diagram illustrating an alternative embodiment of an intraoperative autotransfusion system using an integrated filter;
FIG. 4 is a schematic diagram of a machineless intraoperative autotransfusion system;
FIG. 5 is a schematic diagram of an alternative embodiment of a machines interoperative autotransfusion system;
FIG. 6 is a schematic diagram illustrating an alternative embodiment of an intraoperative autotransfusion system;
FIG. 7 is a schematic diagram illustrating a postsurgical autotransfusion system;
FIG. 8-A is a schematic diagram of a machineless postsurgical autotransfusion system using a water-manometer for vacuum regulation;
FIG. 8-B is a cross-sectional view of a spring-loaded piston system which may be used with the embodiment illustrated in FIG. 8-A to regulate the vacuum pressure;
FIG. 9 is a cross-sectional view of an emboli filter for use in the invention;
FIG. 10 is a schematic diagram of a simplified embodiment of the invention for use during episodes of less bleeding;
FIG. 11 is a schematic diagram of the embodiment illustrated in FIG. 10 in which the blood collection bag is repositioned.
FIG. 12 is a schematic diagram of an alternative embodiment of a simplified version of the invention in which vacuum is applied to the blood collection bag and filtration receptacle; and
FIG. 13 is a cross-sectional view of a suction means for use in the invention.
DETAILED DESCRIPTION OF THE DRAWINGS
FIG. 1 illustrates an embodiment of the invention for use during surgery. In FIG. 1, the location of the wound site is designated generally at 10. The wound site could be a surgically-induced wound or a serious trauma resulting from an accident, such as a gun-shot wound.
When there is bleeding at thewound site 10, the shed blood is aspirated by suction means 12. The suction means 12 generally includes a handle and a suction tip. The suction means 12 is connected tosuction tubing 14. The other end of the suction tubing is connected to theblood inlet port 16 of anemboli filter 18 or cardiotomy reservoir. The emboli filter 18 is enclosed within an emboli filter casing 19. The emboli filter casing is provided with a vacuum connector means 20 near the top of the casing 19. Space between the emboli filter casing 19 and the emboli filter 18 forms a blood reservoir 22. An aperture in the bottom of the emboli filter casing 19 opening into the reservoir 22forms blood outlet 24. To the vacuum connector means 20 is connected avent line 26 which may be connected to a controlledvacuum source 28. Most operating rooms are generally equipped with a vacuum source which can be controlled at any desired value.
The invention provides a method of delivering washing fluid to be mixed with the aspirated blood at a rate in proportion to the flow rate of the aspirated blood. A bag orretainer 30 containing washing fluid is located from about equal in height to the suction means 12 to about two feet below the suction means 12. Awashing fluid line 32 extending from thewashing fluid bag 30 is connected to thesuction tubing 14 by a Y-connector 34. The washing fluid bag is a conventional collapsible plastic bag used for fluid retention. The washing fluid may be any physiological fluid such as normal saline or Ringer's solution. The washing fluid may be mixed with an anticoagulant, such as heparin, in order to prevent clotting of blood in the autotransfusion system.
When there is no bleeding in thewound site 10, the suction means 12 is not exposed to blood and remains open to the atmosphere. During this period, air sucked into thesuction tubing 14 flows into the emboli filter 18, and is then removed through the vacuum connector means 20 via thevent line 26. Due to the aspiration of air through the suction means 12, which offers a very low resistance to flow, the negative pressure in thesuction tubing 14 decreases to almost the level of atmospheric pressure. This decreased negative pressure in thesuction tubing 14 will not be sufficient to lift the washing fluid from thewashing fluid bag 30 into thewashing fluid line 32. In other words, when there is no bleeding, the washing fluid flow rate reduces to zero.
It will be appreciated that by suitably adjusting the flow resistance in thewashing fluid line 32 with respect to the flow resistance in thesuction tubing 14 and suction means 12, the flow rate of washing fluid may be regulated at any desired value. Such resistance may be achieved by varying the diameter of thewashing fluid line 32.
When there is bleeding, the suction means 12 is inserted in the pool of blood to remove it from the wound site in order to keep the wound site clear for surgery. Due to the application of vacuum in thesuction tubing 14, the aspirated blood is transported from thewound site 10 into the emboli filter 18 through thesuction tubing 14. This increases the flow resistance in thesuction tubing 14, which increases the negative pressure in thewashing fluid line 32. Increased negative pressure is then sufficient to lift the washing fluid from thebag 30. The washing fluid will then flow into thesuction tubing 14 through the Y-connector 34 where it is mixed with the aspirated blood.
Diluted blood, or the admixture of blood and washing fluid, then flows into the emboli filter 18 where it is degassified and filtered. The emboli filter may generally be any type of filter which can filter out air from the blood. In a preferred embodiment, as shown in FIG. 9, the emboli filter includes apolyurethane sponge 510 coated with an antifoam silicone compound which assists in the degassification of the aspirated blood. The lower portion of the sponge is covered with aporous filter fabric 512 having a pore size of about 40 microns. Thefabric 512 is hydrophilic and allows only blood to permeate therethrough. Polyester is an exemplar fabric for this use. When polyester is wet, it will not allow permeation of air therethrough unless high transmembrane pressure is applied. The upper portion of thesponge 510 is covered with ahydrophobic fabric 514 which does not allow blood to permeate therethrough, but correspondingly allows air to permeate therethrough. Nylon is an exemplar fabric for this purpose. As the blood/washing fluid admixture enters the emboli filter through theinlet port 516, the blood filters through thesponge 510. Air becomes separated from the blood and rises to the top portion of the filter. Blood is filtered through the bottom portion of the filter, and impurities of a larger size (typically greater than 40 microns) are filtered out. The blood collects in thereservoir 518 associated with the emboli filter. A vacuum connector means 520 is provided to which is attached a vacuum source (not shown). Negative vacuum pressure from the vacuum source vents off air separated out by thepolyurethane sponge 10 and also applies negative pressure to the blood collected in thereservoir 518 to remove air therefrom.
Referring again to FIG. 1, the blood level in the reservoir 22 is detected byultrasonic detectors 60 and 64. The ultrasonic detector 64 at the upper portion of the reservoir detects a high level of blood in the reservoir, and thedetector 60 in the lower portion of the reservoir detects a low blood level.
The invention provides a continuous on-line method of removing impurities from the blood which are below a specified molecular size. Purified blood which has a specified cellular volume fraction (i.e., hematocrit) value is reinfused. A specified cellular volume fraction may be achieved by recirculating the filtered blood exiting from theoutlet port 24. The blood is circulated by means of a roller pump 36 which urges the blood through amembrane filter 38, aflow constrictor 40, a conductivity (i.e., hematocrit) monitor 42, and a recirculation valve 44. The cellular volume fraction of the recirculating blood may be continuously measured using an on-line conductivity monitor 42. Recirculation through the system may be accomplished by any pumping means, including a conventional roller pump 36.
Cellular volume fraction (i.e., erythrocyte count) is measured continuously by the monitor means 42. In a preferred embodiment, the monitor means is a conductivity monitor which constantly measures the conductivity of blood at a specified frequency using two stainless steel electrodes (not shown) at the outlet of themembrane filter 38. Such conductivity monitors 42 are available on the market (e.g., from Sedatelec, Chemin des Muriers, Irigny, France). These electrodes supply a current of ten microamperes to the blood at a frequency of five thousand Hertz. Measured conductivity of blood is known to be proportional to its noncellular volume fraction. Therefore, it noncellular volume is high, more recirculation is needed to remove fluids until a desired amount of cellular blood components remain.
Themembrane filter 38 may be any conventional membrane-type separator with a pore size ranging from 40,000 daltons to 400,000 daltons molecular weight cut off. Such filters are known in the art as ultrafilters. It may be preferable to use a membrane with a pore size not exceeding 100,000 daltons. However, if larger size impurities are to be removed, a filter having a pore size of 400,000 daltons, or a plasma filter having a pore size of up to 0.4 micron (a few million dalton molecular weight cut off) can be used. Which membrane filter is used will depend on the types of molecules or blood components the surgeon wants to maintain in the blood for reinfusion. As blood passes through themembrane filter 38, fluid and other components having a size smaller than that of the membrane pores will be removed as filtrate through thefiltrate port 46. The filtrate may be collected in afiltrate receptacle 48.
As the fluid is removed from the recirculating blood by themembrane filter 38, the cellular volume fraction (i.e., hematocrit) will increase. When the hematocrit of recirculating blood reaches the specified value, as measured by theconductivity monitor 42, the recirculation valve 44 closes to stop the recirculation procedure. The recirculation valve 44 may be a three way shunt valve which intermittently allows blood to flow through the recirculation pathway, and intermittently occludes that pathway thereby allowing the blood to enter thereinfusion pathway 50.
Blood entering the reinfusion pathway at 50 flows through a venous filter 52, avenous valve 54 and areinfusion line 56. The venous filter 52 removes any blood clots from the blood prior to its reinfusion. The blood level in the venous filter 52 may be detected by an ultrasonic detector 58. Thevenous valve 54 normally remains closed (i.e., during recirculation). It opens only when three conditions are met simultaneously. These conditions are: (i) No air bubble must be present in the blood to be infused, as detected by an ultrasonic bubble detector 58; (ii) the level of blood in the reservoir 22 must be above the lower point of the reservoir as monitored by the ultrasonicblood level detector 60; and (iii) the cellular volume fraction of recirculating blood must be equal to or greater than a specified value as monitored by theconductivity monitor 42.
The apparatus as described above provides the patient with his/her own blood which is free of air emboli and which is at a specified cellular volume fraction. The specified cellular volume is to be determined by the attending physician(s) in accordance with the patient's needs.
The embodiment described in FIGS. 1 and 2 provides a simple method of membrane filtration without using any filtrate pump (i.e., a suction pump in the filtrate port 46) or transmembrane pressure difference control. Rather, filtration is accomplished by providing flow constriction means 40 at the outlet of themembrane filter 38. Constriction of the outlet through which blood exits the membrane filter acts to increase transmembrane pressure difference in the membrane filter. Increased transmembrane pressure enhances filtration.Filtrate port 46 is connected to acollapsible filtrate receptacle 48 which collects filtrate (waste) from the membrane filter. A suction pump in connection with thefiltrate port 46 may be used, but one need not be used if the objective is to keep the system as simple as possible. Thus, where a filtrate pump is not used, pressure in the filtrate port is constant and is about equal to atmospheric pressure.
It is well known in the art that membrane filtration rate is dependent on the extent of dilution of the blood (i.e., viscosity, hematocrit, plasma protein concentration). Filtration rate increases with increase in dilution of blood for the same transmembrane pressure difference and shear rate (i.e., blood flow rate). Thus, more fluid will be removed from the blood by membrane filtration when the blood is more diluted. It is also known in the present art that filtration rate can also be increased by increasing shear rate and transmembrane pressure difference.
The embodiment shown in FIGS. 1 and 2 provides a method of increasing transmembrane pressure difference and shear rate by increasing the speed of the recirculation pump in proportion to the amount of fluid to be removed from the blood. The amount of fluid to be removed may be determined from theconductivity monitor 42 located in proximity to the outlet of themembrane filter 38 in the recirculation pathway. If the measured value of cellular volume fraction is below a specified limit (e.g., 35%), then a signal is sent to the speed-control of the recirculation pump 36 to increase its speed to a higher value. In other words, the lower the measured cellular volume fraction, the higher will be the pump speed, transmembrane pressure difference, shear rate, and filtration rate.
Alternatively, filtration may be increased as determined by the level of blood in the reservoir 22. Therefore, when the level of blood rises above the level of the blood level detector 64, the speed of the recirculation pump 36 increases. When the level of blood in the reservoir 22 falls below the blood level detector 64, then the speed of the recirculation pump 36 decreases. As a result, the amount of fluid removed from the blood may also be manipulated by the amount of blood in the reservoir for processing.
It should be noted that prior to the operation of this embodiment of the apparatus, washing fluid containing heparin may be circulated through the apparatus to eliminate all the air bubbles from the system. Thus, at the beginning of the flushing procedure, the cellular volume fraction of fluid circulating through the membrane filter may be almost zero. In such a case, rapid filtration may be falsely triggered by the control unit. As a result the level of fluid in the filter reservoir 22 may drop below the set value as determined byblood detector 60 causing air to be sucked into themembrane filter 38. In order to eliminate air being sucked into themembrane filter 38, thefiltrate port 46 may be closed by afiltrate valve 62 which closes only when the fluid level in the reservoir 22 falls below the level of theblood level detector 60. Thefiltrate valve 62 may also be closed when the cellular volume fraction measured by theconductivity monitor 42 becomes equal to or greater than the specified value.
The embodiment described in FIGS. 1 and 2 is directed to function on a real time basis. That is, purified blood will be returned to the patient within a few minutes of aspirating it from thewound site 10.
The apparatus of this embodiment can be more fully understood with reference to FIG. 2, which is generally a front view of the apparatus described in FIG. 1. The components of FIG. 2 have been described in FIG. 1. The suction means 112 is connected toblood inlet port 116 of the emboli filter 118 bysuction tubing 114. The vacuum connector means 120 of the emboli filtercasing 119 is connected to a controlledvacuum source 128 by avent line 126 so that controlled negative pressure can be applied to aspirate blood from the wound site into theemboli filter 118. Washing fluid is brought into thesuction tubing 114 by increased negative vacuum pressure, as previously described. Thewashing fluid bag 130 is located about two feet below the emboli filter 118 and, washing fluid flows through thewashing fluid line 132 which is connected to thesuction tubing 114 by a Y-connector 134.
Aspirated blood mixed with washing fluid enters the emboli filter 118 via theblood inlet port 116. Filtered blood, free of air and particles larger than 40 microns, is collected in thefilter reservoir 122. This blood is drawn from thereservoir outlet 124 of thereservoir 122 by the recirculation pump 136. The blood is then circulated through themembrane filter 138, aflow constrictor 140, aconductivity monitor 142, and arecirculation valve 144, and it then returns back to thereservoir 122 for recirculation by the recirculation pump 136. Filtrate leaving thefiltrate port 146 is collected in thefiltrate receptacle 148.
Recirculation of blood through themembrane filter 138 is intended to continue until the fluid removed from the blood by filtration becomes at least equal to the amount of fluid that was infused into the blood. This may be done by continuously monitoring the conductivity of the recirculating blood using aconductivity monitor 142 located in proximity to the outlet of themembrane filter 138. When the cellular volume fraction becomes equal to or greater than a specified value, recirculation stops by the closing of therecirculation valve 144, and blood is forced to exit the recirculation pathway at 150.
The processed blood leaves the recirculation pathway at 150 and flows into the venous filter 152 where blood clots, if any, are filtered out. Filtered blood leaves the venous filter 152, passing through the venous valve 154 and proceeds to thevenous reinfusion line 156. Anultrasonic detector 158 may be provided to detect any air bubbles present in the blood flowing through the venous filter. An additional ultrasonic bubble detector which serves as ablood level detector 160 is provided in order to detect air bubbles in the blood contained in thereservoir 122. Similarly, ablood level detector 164 measures a high level of blood in thereservoir 122.
To ensure safety to the patient, processed autologous blood may not be reinfused until the following three conditions are met: (i) The cellular volume fraction of blood, as measured by theconductivity monitor 142, is at least equal to a set value; (ii) the blood level in thefilter reservoir 122 remains above a set value as determined by theblood level detector 160, and (iii) the venous blood in the venous filter 152 does not contain any air bubbles as determined by theultrasonic detector 158. Only when these three conditions are met does the venous valve 154 remain open to allow reinfusion of blood to the patient. Concurrently, therecirculation valve 144 remains closed. However, whenever one of the aforementioned three conditions is not met, the venous valve remains closed and the recirculation valve remains open to allow continued filtration.
The filtration rate through themembrane filter 138 may be controlled by increasing the recirculation pump 136 speed in proportion to the amount of fluid to be removed. The amount of blood which needs to be processed is determined by theblood level detector 164; that is, when the level of blood is above theblood level detector 164, a signal is sent to the recirculation pump 136 to increase in speed. As noted above, increased filtration increases the amount of fluid removed from the blood. Further, that excess fluid needs to be removed can also be determined by the cellular volume content monitored by theconductivity monitor 142. When the cellular volume fraction decreases, more fluid needs to be removed from the blood, and the recirculation pump is signalled to increase speed.
FIG. 3 illustrates an alternative embodiment of the system. As with the previous embodiments, suction means 112 is provided for aspirating blood from the wound site; washing fluid is retained in acollapsible bag 130; the washing fluid is infused by increasing negative pressure into thesuction tubing 114; and admixed blood and washing fluid enter the emboli filter 118 at theinlet port 116. Avacuum source 128 is connected to the emboli filtercasing 119 by avent line 126 attached to the vacuum connector means 120 which supplies the negative pressure for suction.
In this embodiment, themembrane filter 138 is integrated with theemboli filter 118. Themembrane filter 138, in this illustrated embodiment, is positioned below the emboli filter. Filtration across the membrane filter is achieved by a filtration pump (roller pump) 168 which provides negative pressure for filtration. Thefiltration pump 168 may be operated at a constant flow rate of approximately 200 milliliters per minute (ml/min.). However, when the blood level in thereservoir 122 falls below a set level, as detected by theblood level detector 160, thefiltrate pump 168 will stop.
Aninfusion pump 166 infuses blood from thereservoir 122 to the patient via thevenous line 156. Theinfusion pump 166 will infuse blood to the patient only when two conditions are met: (i) The cellular volume fraction of blood measured by theconductivity monitor 142 is above a set value, and (ii) the level of blood in thereservoir 122 is above the level detected by theblood level detector 160.
It will be appreciated that in the embodiment described in FIG. 3, damage to blood is minimized, and the system is significantly simplified, by eliminating blood recirculation between themembrane filter 166 and thereservoir 122. This is made possible by the integration of theemboli filter 118 and themembrane filter 138. The integrated filter may be denominated as an "integrated cascade filter." This integrated filter may be made by potting a bundle of hollow fibers or tubules together and positioning them at the bottom of an emboli filter in such a way that both the emboli filter and the membrane filter are enclosed by a single reservoir. "Potting", as used herein, is a procedure for affixing together a bundle of hollow tubules using an agent such as glue, resin, polymers and the like. Alternatively, the bundle of hollow fibers which comprise the membrane filter portion of the integrated filter may encircle the emboli filter to strain and filter out excess fluid as the blood exits the wall of the emboli filter. The membrane filter may also be a flat membrane shaped like a hollow cylindrical drum positioned proximate to the emboli filter, and may be mechanically rotated (e.g., by motor means) to increase circulation of the blood. Membrane filters of this type are manufactured by Baxter Labs. of Deerfield, Ill.
The embodiments illustrated in FIGS. 4, 5, 10, and 12 are embodiments directed to disposable units which are easily manipulated, positioned, operated, and disposed of after use. It is the objective of these embodiments to present a simplified apparatus for use during intraoperative or post-operative procedures.
As in the previously described embodiments, the apparatus generally includes anemboli filter casing 119 to which is attached avacuum source 128 via avent line 126 of tubing which connects to the emboli filter casing at the vacuum connector means 120. A source of vacuum is readily available in most surgical settings. The vacuum source applies a negative pressure to theemboli filter 118, which is positioned within the emboli filtercasing 119. The negative pressure of the vacuum source should be regulated from about -125 to about -200 mm Hg. Insufficient vacuum will prohibit proper aspiration of blood, and washing fluid, into the system; however, excessive negative pressure will ultimately damage the blood cellular components, and may cause aspiration of blood from thereservoir 122 into thevacuum source 128.
The embodiment of FIG. 4 includes suction means 112 for aspirating blood from the wound site. The suction means 112 is generally comprised of a handle for gripping by the surgeon or medical personnel, and a tip for placement into the blood source formed at the wound site. The handle is connected to a length ofsuction tubing 114 which connects to theblood inlet port 116 of theemboli filter 118. Thesuction tubing 114 may be composed of any flexible material typically used in surgical equipment, including rubber, plastic, and the like.
A flexibleplastic bag 130 containing washing fluid, and anticoagulant if desired, is connected to thesuction tubing 114 via washingfluid line 132 by means of a Y-connector 134. The Y-connector 134 may be positioned along thesuction tubing 114 anywhere from approximately adjacent the suction means 112 to approximately adjacent theblood inlet port 116 of the emboli filter. Thewashing fluid bag 130 must be maintained approximately two feet below the level of the suction means 112. So positioned, the amount of fluid being drawn into thesuction tubing 114 as a result of the negative pressure applied by thevacuum source 128 will approximately equal the amount of blood being aspirated into thesuction tubing 114 from the wound site. It will be recognized that adjusting the height of thewashing fluid bag 130 above or below the above-specified height relative to the suction means 112 will result in more or less washing fluid being drawn into thesuction tubing 114, respectively.
Further, the equal ratio of aspirated washing fluid to aspirated blood may be maintained with an increase or decrease in the suggested height of thewashing fluid bag 130, relative to the suction means 112, coupled with a corresponding decrease or increase in size of the tubing of thewashing fluid line 132.
Aspirated blood and washing fluid mix together at the intersection of washingfluid line 132 and thesuction tubing 114 at the Y-connector 134. The blood/washing fluid admixture is drawn through thesuction tubing 114 by means of negative pressure, and enters into theemboli filter 118. The emboli filter 118 is enclosed within the emboli filtercasing 119 which is comprised of a hard or otherwise suitably non-collapsible material. The space between theemboli filter 118 and the emboli filtercasing 119 defines thereservoir 122. The emboli filter 118 may be any standard filter which has the capability of removing particulate matter and air bubbles. The emboli filter illustrated in FIG. 9, as described above, is preferred. As blood enters theemboli filter 118, large particulates are filtered out and air bubbles are directed to the upper portion of the filter as described above. The negative pressure of the vacuum source draws the air bubbles away from the filter. The filtered blood drains through the filter and collects in thereservoir 122. If any air bubbles remain in the filtered blood retained in thereservoir 122, they are further subjected to negative pressure from the vacuum source, and are drawn into thevent line 126 thereby.
It is contemplated that the components of the embodiment shown in FIG. 4 may preferably be attached to a standard I.V. pole, or similar device. The emboli filter 118 should be placed on the I.V. pole approximately six feet above the ground. At that level, the emboli filter is approximately two to three feet above the level of the patient on the operating table. The emboli filter may be positioned from about two feet to about five feet above the relative height of the patient. Aspiration of blood from the would site is maximized at that range of heights. That is, an average negative pressure of -120 mm Hg can raise a column of blood approximately five feet; therefore, the relative height of the emboli filter above the patient should not exceed five feet. Flow resistance in the conduit is also affected by the diameter of the conduit. Therefore, thesuction tubing 114 should range in diameter from about 5 mm to about 20 mm, with a preferred diameter of 10 mm. Filtered blood collected in thereservoir 122 flows downwardly to themembrane filter 138 via theconduit 139, which is interconnected between the emboli filtercasing 119 at theoutlet port 124 and themembrane filter 138. The emboli filter may be positioned from about six feet to about nine feet above the membrane filter, and a preferred relative height is about seven feet above the membrane filter. At that height, blood is able to flow by gravity through theconduit 139 to themembrane filter 138, and there is sufficient negative pressure exerted on theconduit 139 to allow back-flow of blood for the filtration process, as described below. To maximize flow through theconduit 139, the diameter of the tubing should be from about 4 mm to about 8 mm with a preferred diameter of 6 mm. The length ofconduit 139 should be from about six feet to about nine feet.
Themembrane filter 138 is located approximately at ground level to about one foot above ground level on the I.V. pole. Hydrostatic forces and gravity force the blood to pass through themembrane filter 138 and into theblood collection bag 170 via thesecond conduit 141, interconnected between themembrane filter 138 and theblood collection bag 170. The blood collection bag is made of flexible plastic, or similar material, which has been evacuated of air prior to use. Theblood collection bag 170 is preferably positioned approximately five feet above the height of the membrane filter. The diameter ofsecond conduit 141 may range from about 4 mm to about 10 mm, with a preferred diameter of 6 mm. Theblood collection bag 170 has a port means 176 from which the blood may be infused back into the patient when the bag becomes full.
As the blood passes through themembrane filter 138, it passes through the small porous tubules of the membrane filter which separates out excess fluid and very small particles. The filtrate which is separated from the blood exits themembrane filter 138 atfiltrate port 146, and enters into thefiltrate receptacle 148 via afiltration line 145 connecting thefiltrate receptacle 148 to thefiltrate port 146. Avacuum source 172 may optionally be connected to thefiltrate receptacle 148 by means oftubing 174 connected to thevacuum port 149 of thefiltrate receptacle 148. The filtrate receptacle is correspondingly comprised of a rigid material, such as hard plastic or the like. The negative pressure applied to thefiltrate receptacle 148 may range from about -60 mm Hg to about -200 mm Hg.
It may be appreciated that when there is bleeding at the wound site, the tip of the suction means 112 placed into the pool of blood causes negative pressure to increase, thereby causing blood and washing fluid to be sucked into thesuction tubing 114 and into theemboli filter 118. When bleeding slows or stops, the lack of fluid being aspirated into thesuction tubing 114 causes the negative pressure to drop to approximately -80 mm Hg, and no fluid is aspirated into theemboli filter 118. During this period of reduced negative pressure, blood and washing fluid which has been aspirated previously into the emboli filter, filters therethrough and collects in thereservoir 122. By gravity, it then passes throughconduit 139 into themembrane filter 138. Hydrostatic pressure further forces the blood through themembrane filter 138 into theblood collection bag 170. If avacuum source 172 has been connected to thefiltration receptacle 148, the negative pressure thus applied acts to draw filtrate from themembrane filter 138, and may collaterally act to urge blood from thereservoir 122 to theblood collection bag 170. The amount of filtration which takes place at this time is dependent upon the transmembrane pressure difference (TMP). The TMP is dependent upon the height of thereservoir 122, on the height of theblood collection bag 170, and the level of negative pressure.
When blood is present at the wound site for aspiration, and is aspirated into the system via the suction means 112, negative pressure increases. Concurrently acting to aspirate blood and washing fluid into the emboli filter, the negative pressure also acts to draw the blood from theblood collection bag 170 back through themembrane filter 138, and into thereservoir 122. When bleeding subsides, and there is a concomitant drop in negative pressure, the blood passes back down through themembrane filter 138 and into theblood collection bag 170. With each pass through the membrane filter, more fluid and small particles are removed as filtrate.
When a sufficient amount of blood has collected in theblood collection bag 170, theblood collection bag 170 can be removed from thesecond conduit 141, and can be replaced by another flexible bag from which all the air has been evacuated. The blood collected in the removed bag may then be infused back into the patient fromoutlet port 176. Alternatively, theblood collection bag 170 may remain in place for infusion to the patient. In that situation, the negative pressure supplied to the system by thevacuum source 128 must remain low. Preferably, a clamp should be placed on thesecond conduit 141 to prevent blood from entering or exiting theblood collection bag 170.
Before reinfusing, the amount of fluid collected in thefiltrate receptacle 148 should be compared with the amount of washing fluid which was infused into the aspirated blood. The amount of fluid in thefiltrate receptacle 148 should be roughly equal to the amount of fluid infused into the system. If it appears that less fluid has been recovered than was infused into the system, the blood may be continuously circulated through themembrane filter 138 by periodically applying pressure to thesuction tubing 114 at point AA, as shown in FIG. 4. By applying pressure, such as by squeezing thesuction tubing 114 between the thumb and forefinger, negative pressure increases in theemboli filter 118 and blood from theblood collection bag 170 is urged through themembrane filter 138 toward thereservoir 122. When the pressure is released, the negative pressure decreases again, and gravity causes the blood to circulate through themembrane filter 138 toward theblood collection bag 170. By intermittent application of pressure, the blood may be effectively recirculated through the membrane filter until a sufficient amount of fluid has been removed. Pressure may also be applied to thesuction tubing 114 by use of a mechanical clamp.
FIG. 5 illustrates an alternative embodiment to the simple configuration shown in FIG. 4. This embodiment presents a different method of introducing washing fluid into the aspirated blood for the washing procedure. As with the previously described embodiments, blood is aspirated from the wound site by suction means 112 under negative pressure supplied by avacuum source 128 connected to the emboli filtercasing 119. The aspirated blood is directed to the emboli filter 118 bysuction tubing 114, and the blood enters the emboli filter 118 at theblood inlet port 116. Blood is immediately filtered through the emboli filter 118 as described above, and the blood is collected in thereservoir 122. In this embodiment, however, the filtered blood is thereafter directed, by gravity, to ablood collection bag 170, which is positioned approximately one to three feet above the ground on the I.V. pole (not shown). Blood flows from thereservoir 122 to theblood collection bag 170 via aconduit 139 which is interconnected between theoutlet port 124 of the emboli filtercasing 119 and theblood collection bag 170. The relative positions of thewashing fluid bag 130, theemboli filter 118, themembrane filter 138, and the suction means 112 are those described hereinabove with respect to FIG. 4.
Aclamp 182 may be placed on thetubing 178, which interconnects theblood collection bag 170 and themembrane filter 138, below theblood collection bag 170 to prevent blood from circulating further through the system. Theblood collection bag 170 may contain a precalculated amount of an anticoagulant to prevent clotting of blood accumulated therein. If necessary, the blood may be reinfused to the patient at this point through thereinfusion port 176. The emergency of the situation may require that the blood be reinfused to the patient without further filtration.
Under less exigent conditions, the blood may be filtered further by allowing filtered blood to collect in theblood collection bag 170. When theblood collection bag 170 is partially full, theclamp 182 may be released or removed from thetubing 178 interconnected between theblood collection bag 170 and themembrane filter 138. Removal of theclamp 182 allows washing fluid retained in thewashing fluid bag 130, which is positioned above themembrane filter 138, to pass through themembrane filter 138 and into theblood collection bag 170. The washing fluid is generally urged into the blood collection bag through gravitational forces by manipulating the height of the washing fluid bag means 130 relative to theblood collection bag 170. That is, a medical attendant may raise thewashing fluid bag 130 above the level of theblood collection bag 170 to urge washing fluid into theblood collection bag 170, followed by lowering thewashing fluid bag 130 below the level of theblood collection bag 170 to urge the admixed blood and washing fluid back into thewashing fluid bag 130. During this time, thefiltrate clamp 184 should remain closed to prevent filtration of the washing fluid.
Recirculation of the blood/washing fluid admixture may be accomplished by sequentially lowering and raising the height of thewashing fluid bag 130 in relation to theblood collection bag 170. The admixture of blood and washing fluid is thereby made to circulate between theblood collection bag 170 and thewashing fluid bag 130 via themembrane filter 138. During this period of recirculation, thefiltrate clamp 184 located on thefiltration line 145 is removed, and excess fluids and unwanted components removed by themembrane filter 138 exit via thefiltrate port 146 into thefiltration line 145 and into thefiltrate receptacle 148. Filtration may be enhanced by application of a vacuum pressure by attaching avacuum source 172 to thefiltrate receptacle 148 via avacuum line 174.
When the amount of fluid in thefiltrate receptacle 148 roughly equals the amount of fluid which was originally in thewashing fluid bag 130, thefiltrate clamp 184 may be replaced on thefiltration line 145, and the resulting filtered blood is urged into theblood collection bag 170 by manipulation of thewashing fluid bag 130 to an elevated height. The filtered blood is thereby urged, by gravitational forces, into theblood collection bag 170. Theclamp 182 below theblood collection bag 170 is secured ontubing 178 and the blood may then be reinfused to the patient from thereinfusion port 176. Alternatively, the blood may be urged into thewashing fluid retainer 130, a clamp (not shown) may be connected to the tubing 180 interconnected between the washingfluid bag 130 and themembrane filter 138, below theblood collection bag 170, and the blood may then be infused fromport 133.
It may be appreciated that the embodiments shown in FIGS. 4 and 5 are particularly useful in processing blood from a wound site in a batch process when bleeding is intermittent or slow. However, the embodiments of FIGS. 4 and 5 are configured such that blood cannot be continuously processed, or infused back to the patient, when bleeding is constant or heavy because the increased negative pressure during aspiration causes blood collected in theblood collection bag 170 to back up into thereservoir 122. As a result, it is difficult to collect blood continuously in the blood collection bag.
The embodiments illustrated in FIGS. 10 and 12, therefore, are configured for use during heavy or constant bleeding episodes when blood needs to be infused back into the patient immediately, with or without washing the blood with washing fluid. As shown in FIG. 10, suction means 112 for aspirating blood from the wound site is connected, viasuction tubing 114, to the emboli filter 118 at theblood inlet port 116. Theemboli filter 118, as with the previously described embodiments, is positioned within an outer emboli filtercasing 119 comprised of a rigid material, such as plastic or the like. Avacuum source 128 is connected to the emboli filtercasing 119 via avent line 126 of tubing which connects to the vacuum connector means 120 of the emboli filtercasing 119. Negative pressure is thereby supplied to the emboli filter ranging from about -125 mm Hg to about -200 mm Hg.
The apparatus of FIG. 10, like those of FIGS. 4 and 5 is preferably attached to an I.V. pole or the like. Theoutlet port 124 of the emboli filtercasing 119 should be maintained at least six feet above the ground level. Theconduit 139, interconnected between theoutlet port 124 and themembrane filter 138, should be at least 5.50 feet in length. Themembrane filter 138 and theblood collection bag 170 should be maintained at or near ground level.
In this embodiment, blood from the wound site is aspirated directly into the emboli filter 118 without being admixed first with washing fluid. The aspirated blood enters the emboli filter 118 where large particulates and air bubbles are removed, as described above. Blood drains from the emboli filter 118 and collects into thereservoir 122 formed between the emboli filtercasing 119 and theemboli filter 118.
By gravitational force, the blood collecting inreservoir 122 travels downconduit 139, through themembrane filter 138, and into theblood collection bag 170 via thesecond conduit 141 interconnected between themembrane filter 138 and theblood collection bag 170. It should be noted that thesecond conduit 141 may be bifurcated so as to enable the attachment of more than one blood collection bag thereto. Theblood collection bag 170 is preferably a flexible material, such as plastic or rubber, and may be empty, or may be pre-filled with washing fluid.
If the surgeon predicts that blood infusion to the patient must take place immediately upon aspiration, theblood collection bag 170 will not be pre-filled with washing fluid. Instead, filtered blood descending into theblood collection bag 170 from thereservoir 122 may be infused immediately into the patient by connecting an infusion line to thereinfusion port 176 of theblood collection bag 170.
When time permits, and washing of the blood is desired, theblood collection bag 170 is pre-filled with washing fluid. The blood collection bag may be pre-filled with washing fluid prior to surgery by placing the suction means 112 into a source of washing fluid and aspirating a desired amount of fluid. The washing fluid filters through the emboli filter and descends through theconduit 139 into theblood collection bag 170. During this time,filtrate clamp 184 must be in place on thefiltration line 145 to prevent loss of fluid into thefiltration receptacle 148. Theblood collection bag 170 may also be pre-filled with washing fluid prior to its attachment to thesecond conduit 141.
As blood is aspirated through the suction means 112, negative pressure (about -120 mm Hg) typically forces the washing fluid from theblood collection bag 170 through themembrane filter 138 into theconduit 139. However, negative pressure of -120 mm Hg can only lift fluid to a height of about 5.3 feet in aconduit 139 having a diameter of about 6 mm. As aspirated blood enters theemboli filter 118 and filters into thereservoir 122, the blood thereafter descending through theconduit 139 begins to mix with washing fluid therein.
A negative pressure of -120 mm Hg can only raise blood 5.04 feet when the diameter of the conduit is about 6 mm. Therefore, the height of theoutlet port 124 of the emboli filtercasing 119 must be kept at a height proportional to the negative pressure applied by thevacuum source 128. That is, the blood level inconduit 139 achieves a height of 5.04 feet above the ground level, the negative pressure equalizes the gravitational force exerted on the column of blood. Since the length of the conduit is greater than at least six feet, the force of blood descending from thereservoir 122 through theoutlet port 124 into theconduit 139 applies additional hydrostatic pressure thereby causing the blood to flow downwardly in theconduit 139. The greater the height of the emboli filtercasing 119, the greater will be the blood flow downwardly through theconduit 139. However, the upper limit of the height of the emboli filter 118 is defined by the relative height between theemboli filter 118 and the surgical table. That is, with an applied pressure of -120 mm Hg, only 5.04 feet of blood can be raised. Therefore, in order to facilitate the aspiration of blood from the wound site into theemboli filter 118, the surgical table or wound site cannot be more than 5.04 feet below the height of the emboli filter.
Mixture of the blood with washing fluid can be enhanced by raising the level of theblood collection bag 170 to a height of approximately six feet above the ground, as illustrated in FIG. 11. Blood and washing fluid will flow back through themembrane filter 138 and partially into theconduit 139. This mixing can take place even during aspiration of blood since the gravitational force in theconduit 139 is still sufficient to force blood downwardly. When the blood and washing fluid have been mixed sufficiently, thefiltrate clamp 184 on thefiltration line 145 is removed so that filtration may begin. As the blood passes through themembrane filter 138, excess fluids and very small particles are removed. The filtrate flows out from themembrane filter 138 to thefiltrate receptacle 148 through thefiltration line 145 interconnected therebetween.
When sufficient fluid has been removed from the blood, as determined by comparing the amount of fluid observed in thefiltrate receptacle 148 to the amount of washing fluid which was originally placed in theblood collection bag 170, thefiltrate clamp 184 is replaced on thefiltration line 145. The blood is then collected back into theblood collection bag 170 by lowering the bag to the ground level. Another blood collection bag is attached to the bifurcated line of thesecond conduit 141 at connection means 198. Theblood collection bag 170 is then removed from thesecond conduit line 141 by applying pressure to thesecond conduit 141. Blood may then be infused to the patient by attaching an infusion line to theinfusion outlet port 176 of the fullblood collection bag 170.
FIG. 12 presents an alternative embodiment for collecting purified blood wherein theblood collection bag 170 is connected to a source of negative pressure. Thefiltrate receptacle 148 is also connected to a source of negative pressure. As a result, theblood collection bag 170 does not need to be raised and lowered manually to admix and filter the blood and washing fluid through themembrane filter 138.
In FIG. 12, blood is aspirated from the wound site via the suction means 112, and blood is carried to the emboli filter 118 by thesuction tubing 114. As in previously described embodiments (FIGS. 4 and 5), awashing fluid bag 130, which is maintained at a level approximately two feet below the level of the suction means 112, is connected to thesuction tubing 114 by a Y-connector 134. Washing fluid is lifted from the washingfluid bag 132 by negative pressure and is carried through thewashing fluid line 132 to thesuction tubing 114 at the Y-connector 134. There, washing fluid is admixed with aspirated blood. The admixture of blood and washing fluid is aspirated into the emboli filter 118 where it is filtered and collected in thereservoir 122.
As in the embodiment of FIG. 10, the emboli filtercasing 119, and theoutlet port 124, should be kept approximately six feet above ground level. themembrane filter 138 should be kept at or about ground level. The filtered blood collecting in thereservoir 122 descends through theconduit 139, into themembrane filter 138, through thesecond conduit 141, and into theblood collection bag 170.
Occasionally, blood descending through theconduit 139 may contain air bubbles which are not filtered out by theemboli filter 118, or by application of negative pressure upon the emboli filtercasing 119. When large air bubbles become trapped in theconduit 139, the average density of the blood and air in the tube decreases, thereby decreasing the flow of blood in theconduit 139. To prevent the entrapment of bubbles, bubble traps 232, 234 are integrated into theconduit 139 to remove the air. Eachbubble trap 232, 234 is subjected to the negative pressure from thevacuum source 128 as a result of being in communication with the emboli filtercasing 119 through avent line 236, 238 interconnected between thebubble trap 232, 234 and avent tube 230 disposed within the emboli filtercasing 119. Thevent tube 230 is open at its upper end to the upper portion of thereservoir 122, which is most significantly subjected to vacuum pressure. With the open end of thevent tube 230 disposed at the upper portion of thereservoir 122, it is unlikely that blood will enter thevent tube 230 opening.
The bubble traps used in the embodiment may be standard bubble traps, typically used in hemodialysis equipment, which are comprised of an expansion chamber. The expansion chamber of the bubble trap has three openings: an inlet through which blood may enter, an outlet through which blood may exit, and an opening for venting air therethrough. A plurality of bubble chambers may be disposed along the length of theconduit 139 in order to prevent bubble entrapment along its length.
As the admixture of blood and washing fluid passes through themembrane filter 138, excess fluids are removed from the admixture. It is understood that thefiltrate clamp 184 on thefiltration line 145 is in the open position during this time to allow filtrate draining from themembrane filter 138 to exit through thefiltration line 145 into thefiltrate receptacle 148. Thefiltrate receptacle 148 is a non-collapsible container to which vacuum pressure may be applied. As illustrated in FIG. 12, the filtrate receptacle may be attached to thesame vacuum source 128 which is connected to the emboli filtercasing 119. Thevacuum source 128 andfiltrate receptacle 148 are interconnected by avacuum line 242.
Negative vacuum pressure may be applied to thefiltrate receptacle 148 in order to enhance filtration through themembrane filter 138. If connected to thesame vacuum source 128 as that to which the emboli filtercasing 119 is connected, the vacuum pressure applied to thefiltrate receptacle 148 is to be regulated by means of a regulator valve 244 to maintain a lower degree of pressure than is provided to the emboli filter casing 119 (i.e., 120 mm Hg). If a plasma filter is being used, the negative pressure applied should be from between about -60 mm Hg to about -120 mm Hg. If an ultrafilter is being used, the negative pressure applied should be from between about -90 mm Hg to about -200 mm Hg. Pressure applied to thefiltrate receptacle 148 may be determined by apressure indicator 246 on thevacuum line 242. It may also be noted that when negative pressure increases during aspiration of bleeding, the negative pressure to thefiltrate receptacle 148 correspondingly increases as a result of being interconnected to thesame vacuum source 128. When negative pressure decreases during little or no aspiration of blood, the vacuum pressure in thefiltrate receptacle 148 correspondingly decreases. Therefore, filtration increases when blood is being actively aspirated, and filtration decreases when blood is not being aspirated.
In this embodiment, more than one blood collection bag is provided so that infusion can take place from one bag while the other bag is filling with blood. Further in this embodiment, both blood collection bags, which are non-collapsible, are connected to a vacuum source, or to thesame vacuum source 128 to which the emboli filtercasing 119 is attached. Thevacuum line 210 to thecollection bags 170 and 214 is connected to thevent line 126 which is connected to the emboli filtercasing 119. Thevacuum line 210 to thecollection bags 170, 214 is bifurcated, by means of a Y-connector or similar device, into separate vacuum lines to each blood collection bag. The separate vacuum line to each blood collection bag is fitted with a two-way valve 212, 220 which can either supply vacuum pressure to the individual blood collection bag, or can produce atmospheric pressure by closing the valve to the negative pressure. Eachvalve 212, 220 is equipped with aconventional air filter 240, 241 which eliminates bacteria, viruses, and other particulate matter from entering the blood collection bag when atmospheric pressure is introduced.
Thesecond conduit 141 is bifurcated, by means of a Y-connector or similar device, to provide a separate pathway for blood to each separateblood collection bag 170, 214. Each bifurcation of theconduit 141 is equipped with a shut-offvalve 216, 218. In operation, the shut-offvalve 218 to the "stand-by bag" 214 is maintained in the closed position to prevent blood from entering into the stand-bybag 214 while blood is being collected in the otherblood collection bag 170.
Blood filtering through the system enters into theblood collection bag 170 as a result of the shut-offvalve 216 associated with thatblood collection bag 170 being in the open position. During collection of blood in theblood collection bag 170, vacuum pressure is applied throughvacuum line 210 toblood collection bag 170 only. When thebag 170 has filled with a sufficient amount of blood for infusion, the shut-offvalve 216 is closed to prevent entry of any more blood into thatblood collection bag 170. The two-way valve 212 is positioned to terminate application of negative pressure to theblood collection bag 170, and atmospheric pressure is thereby produced in the bag. Blood may then be infused to the patient by connecting an infusion line (not shown) to theoutlet port 176 of theblood collection bag 170.
During infusion fromblood collection bag 170, the shut-offvalve 218 associated with the stand-bybag 214 is opened, and blood begins to fill the stand-bybag 214. The two-way valve 220 to the stand-by bag is positioned so that negative pressure is applied to thebag 214.
Theblood collection bags 170, 214 are preferably positioned at about five to about six feet above the ground level. If the same amount of negative pressure is applied to bothblood collection bags 170, 214 and the emboli filtercasing 119, theblood collection bags 170, 214 may be maintained at a height below the emboli filtercasing 119. If greater negative pressure is applied to theblood collection bags 170, 214 than is applied to the emboli filtercasing 119, aspirated blood will flow from thereservoir 122 to theblood collection bags 170, 214 regardless of the relative height of thebags 170, 214.
It is contemplated by the configuration in FIG. 12 that blood may generally be filtered of excess fluids by a single passage of blood from thereservoir 122 to theblood collection bag 170, 214. However, if it is determined that more fluids need to be removed from the blood, the blood collected in theblood collection bag 170, 214 may be recirculated through themembrane filter 138. For that purpose, acollapsible reservoir bag 224 is provided which connects to theconduit 139, in proximity to themembrane filter 138 by means of atube 223. Aclamp 222 connected to thetube 223 is closed during typical operation to prevent blood from entering thereservoir bag 224. However, when further filtration of fluids is required, theclamp 222 is opened thereby allowing blood to flow into thereservoir bag 224. Blood is urged from theblood collection bag 170, 214 into thereservoir bag 224 by sequentially applying negative pressure and atmospheric pressure to the blood collection bag by manipulation of the two-way valve 212, 220. That is, by producing atmospheric pressure in the blood collection bag, blood is forced from the blood collection bag to thereservoir bag 224. When negative pressure is restored to the blood collection bag, blood will then flow from thereservoir bag 224 back into the blood collection bag. Filtration in themembrane filter 138 takes place with each pass of the blood between theblood collection bag 170, 214 and thereservoir bag 224.
As an alternative to supplying washing fluid to the aspirated blood from the washingfluid bag 130, or when extra washing fluid may be required, washing fluid may be introduced into theblood collection bags 170, 214 atinlet port 226, or may be introduced into thereservoir bag 224 throughinlet port 228.
FIG. 6 illustrates an alternative embodiment of the system described in FIG. 4. It is contemplated that the embodiment of FIG. 6 retains the mobility of the embodiment of FIG. 4 inasmuch as it may be attached to an I.V. pole or similar apparatus. However, the embodiment of FIG. 6 is more mechanized as a result of incorporating into the system apush button control 186 on the suction means 112, anelectromagnetic tubing clamp 188 located on thesuction tubing 114 which is in electrical communication with thepush button control 186, an ultrasonicblood level detector 158 located on theblood collection bag 170, aconductivity monitor 142 at thereinfusion line 156, a blood infusion pump (roller pump) 166, and a filtration pump (roller pump) 168. It is intended that the same relative heights of the components of the apparatus will be maintained as described hereinabove with respect to FIGS. 4, 5 and FIGS. 10 and 12 hereinafter.
When the surgeon wants to aspirate blood from the wound cavity, thepushbutton 186 located on the suction means is activated by the surgeon's thumb pressure. As long as thepushbutton 186 remains activated, thetubing clamp 188 remains open, allowing a mixture of blood and washing fluid to flow into theemboli filter 118. The filtered blood/washing fluid admixture then flows into theblood collection bag 170 by force of gravity via themembrane filter 138.
When there is no bleeding, thepush button control 186 remains inactivated. During this period, thetubing clamp 188 located on thesuction tubing 114 periodically opens and closes thesuction tubing 114 at a predetermined interval (e.g., every one minute). Because of the alternating negative pressure and positive (i.e., atmospheric) pressure in thereservoir 122 due to the closing and opening of thetubing clamp 188, blood is caused to circulate through themembrane filter 138 between thereservoir 122 and theblood collection bag 170. Filtration takes place during this recirculation process.
Filtration in themembrane filter 138 illustrated in FIG. 6 may be enhanced by the association of afiltration pump 168 with thefiltration line 145 leading to the filtrate receptacle (not shown). Thefiltration pump 168 operates at a constant flow rate of about 200 ml/min., as long as two conditions are met: (i) the blood level in theblood collection bag 170 must remain above the level detected by the ultrasonicblood level detector 158, and (ii) the cellular volume fraction as measured by theconductivity monitor 142 must remain below a set value. When these two conditions are not met, thefiltration pump 168 will stop.
Conversely, theblood infusion pump 166 will operate at a predetermined constant flow rate when the measured cellular volume fraction, as determined by theconductivity monitor 142, remains above a set value, and the blood level in theblood collection bag 170 remains above the set value as detected by the ultrasonicblood level detector 158.
The embodiment of FIG. 6 further provides a method of neutralizing the anticoagulant (e.g., heparin) present in the blood returning to the patient. The concentration of heparin in the blood can be expected to be about thirty percent of the concentration of heparin in the washing fluid as a result of the filtration process. Substances which selectively neutralize anticoagulants are well known. For example, heparin may be neutralized by protamine. The amount of protamine, or other similar neutralizing substance, in the neutralizer retainer means 190 is predetermined by the amount of anticoagulant which is originally placed in the washing fluid, and by the expected concentration of anticoagulant in the blood. The anticoagulant neutralizer solution retained in the retainer means 190 is fed into thereinfusion line 156 by way of aneutralizer feed line 192. The neutralizer is fed into thereinfusion line 156 at a rate equal to the reinfusion rate of the blood. This may be accomplished by providing a twochannel roller pump 166 instead of a single channel roller pump. One channel may be used for blood reinfusion and the other channel for the neutralizer. The ratio between the blood and the neutralizer flow rates may be varied by using different tubing sizes for theblood reinfusion line 156 and theneutralizer feed line 192.
The embodiments illustrated in FIGS. 7 and 8 are embodiments which are designed for use post-surgically. That is, they are designed to aspirate blood from a closed wound site into which has been placed a drainage tube in expectation of postoperative bleeding. In FIG. 7, the closed wound site is generally designated at 300. The closed wound site may be located anywhere where surgery has been performed on the body including the pleural cavity, chest cavity or abdomen.Drainage tubing 310 has been inserted at the closed wound site by the surgeon in order to drain out any blood.
The embodiment in FIG. 7 is designed to provide a controlled amount of washing fluid to the drainage tubing, or it may be injected into the closed wound site using a double lumen chest drainage tubing. Washing fluid contained in washingfluid bag 320 may or may not contain anticoagulant. For example, mediastinal blood is reported to be free of fibrinogen, a main ingredient of blood clots and anticoagulant may not be necessary as a result. Washing fluid is pumped from the washingfluid bag 320 by pump means 322, such as a roller pump. The washing fluid is urged thereby into thedrainage tubing 310, or into the closed wound site 300 if a double lumen drainage tube is used, through the washing fluid line 324 at a controlled rate.
The aspirated blood is mixed with the washing fluid in thesuction tubing 326. Alternatively, the blood and washing fluid which is admixed at the wound site is aspirated into thesuction tubing 326. Thesuction tubing 326 terminates at theinlet port 328 of emboli filter 330. The aspirated blood which is diluted with washing fluid is filtered through the emboli filter 330 to remove large particulates and air bubbles from the blood. As illustrated in FIG. 7, the emboli filter may be configured with amembrane filter 336 as an integrated unit, or cascade filter, as previously described with respect to FIG. 3.
The blood level in the reservoir 314 is maintained above a pre-set limit by monitoring the blood level using an ultrasonic air detector 350. If the blood level falls below the level of the ultrasonic air detector 350, anair vent pump 352 connected to avent line 354 exiting the reservoir 314 is activated to pump out air from the reservoir 314. Theair vent pump 352 is only activated when the blood level falls below the pre-set limit. This procedure prevents air from being introduced into the filtered blood.
Blood which has been filtered through the emboli filter 330 is then filtered through amembrane filter 336 which is located beneath the emboli filter 330 as part of an integral unit. The embodiment of FIG. 7 illustrates employment of the same integrated "cascade" filter which is illustrated in FIG. 3. Washing fluid and other excess fluids are separated from the blood by themembrane filter 336. The filtrate is drained into thefiltrate receptacle 346 by means of thefiltration line 342. Filtrate exiting from themembrane filter 336 may be drawn by afiltrate pump 344 so that the filtrate may be collected in thefiltrate receptacle 346. During the membrane filtration process, the washing fluid that was injected into thedrainage tubing 310 or closed wound site 300 will be removed from the blood. The filtrate may also contain other impurities present in the blood such as activated coagulation factors, plasma hemoglobin, fibrin degradation products, and lipids. Themembrane filter 336 may have a pore size cut-off ranging from 40,000 daltons to a few millions of daltons depending upon the size of impurities to be removed from the blood.
The volume of filtrate removed and the volume of washing fluid injected into blood may be roughly equalized by operating thewashing fluid pump 322 andfiltrate pump 344 at the same speed, and using the same diameter of tubing for the washing fluid line 324 and thefiltrate line 342.
Filtered blood exits from theintegrated membrane filter 336 and is carried via aconduit 332 to the blood collection bag 338. Movement of filtered blood through theconduit 332, and ultimately the rate of reinfusion, is accomplished by operation of thereinfusion pump 334. When a suitable amount of blood is collected in the blood collection bag 338, it may be reinfused to the patient, by gravity flow, by attaching a second receptacle (not shown) to theport 340 of the blood collection bag 338 without detaching the blood collection bag 338 from the apparatus. The second receptacle is positioned at a height above the patient suitable for obtaining gravity flow from the second receptacle into the patient. A filter (not shown) having an approximate pore size of 40 microns may be interconnected between the blood collection bag 338 and the second receptacle for further filtration of the blood prior to reinfusion. Alternatively, the filtered blood collected in the blood collection bag 338 may be continuously reinfused to the patient by connecting a reinfusion line to theport 340.
When the threeroller pumps 322, 334, 344, which are driven by a single motor and gear unit (i.e., it may be referred to as a three channel roller pump), are operated at the same speed, the flow rates of washing fluid through thewashing fluid pump 322 and that of filtrate through thefiltrate pump 344 may be made to be exactly equal. At the same time, the flow rate through thereinfusion pump 334 may be made equal to the bleeding rate.
Bleeding rate in the closed wound site varies with time. The embodiment illustrated in FIG. 7 is capable of determining the transient variation of bleeding rate and can process the blood accordingly. Because thewashing fluid pump 332 and thefiltrate pump 344 operate at the same speed, negative pressure is automatically created in the closed wound site 300 by operation of thereinfusion pump 334. Negative pressure induces the mixture of aspirated blood and washing fluid to flow towards theemboli filter 330. The magnitude of the negative pressure is proportional to the speed of thereinfusion pump 334 and inversely proportional to the bleeding rate. It is known in the art that the negative pressure must be kept below -20 cm of water. A negative pressure sensor andpressure control unit 348 may be provided in order to control the negative pressure in thedrainage tube 310 around -20 cm of water.
When the bleeding in the closed wound site 300 decreases, the negative pressure may exceed the set maximum value (e.g. -20 cm water), and the speed of thereinfusion pump 334 is accordingly reduced by thecontrol unit 348 until the measured pressure remains below the maximum value. It should be noted that when the speed of thereinfusion pump 334 is reduced, the speeds of theother pumps 322 and 344 will be reduced proportionately since they are powered by the same motor and gear unit.
If bleeding in the closed wound site 300 increases, the negative pressure in thedrainage tube 310 decreases below the set value (i.e., -20 cm of water), and thepressure control unit 348 accordingly increases the pump speed until the negative pressure approaches the set value. By this control mechanism, all the pump speeds (reinfusion pump 334, washingfluid pump 322, and filtrate pump 344) are automatically adjusted to the bleeding rate, while keeping the negative pressure in the drainage tube within the safe value of -20 cm of water.
It will be appreciated that blood does not come in contact with air during the aspiration process described above thereby totally eliminating blood-air interaction and protein denaturation. The blood-air interface is completely eliminated in the apparatus by flushing it with normal saline or Ringer's solution before attaching the apparatus to the drainage tube at the wound site. Also, because the blood collection bag 338 is a conventional collapsible plastic bag into which vacuum has been applied during its sterilization, no air comes in contact with the blood. It will be appreciated that the elimination of blood-air interface minimizes protein denaturation and eliminates potential dangers of air emboli.
The embodiment of FIG. 8-A presents an alternative embodiment of the invention for use post-surgically. The illustrated embodiment does not depend upon any capital equipment (i.e., pumps, transducers, sensors, electronic controllers and microprocessors), but is dependent only upon a conventional vacuum source available in any operating room, surgical unit or post-surgical management unit (e.g., intensive care unit).
As shown in FIG. 8-A, blood is aspirated from the closed wound site via thedrainage tubing 310 under accurately controlled negative pressure. Thedrainage tubing 310 integrates withsuction tubing 326 which terminates at theinlet port 328 of a conventionalemboli filter 330. A conventional one-way valve, such as aflap valve 370 may be provided in thesuction tubing 326 in order to prevent reverse flow of blood or air to the closed wound site in case of accidental failure of the vacuum source.
Thevent line 126 is connected to an embolifilter vent line 372 which is in turn connected to the reservoir 314 associated with theemboli filter 330. Thevent line 126 is connected to avacuum source 128. The amount of vacuum may be regulated, in part, by regulator valve means, such as a conventional water-manometer 378, as shown. Thevent line 126 is connected to water-manometer line 374 to interconnect the water-manometer to the vacuum source. Amicroporous filter 376 of approximately 0.8 micron pore size (e.g., as made by Millipore Corp., MA.) is associated with the emboli filtervent line 372 in order to prevent transfer of bacteria or viruses into the emboli filter from thevent line 126 in case of accidental failure of thevacuum source 128.
A conventional water-manometer 378 is used in this embodiment to accurately control the required negative pressure in thevent line 126. The water manometer may comprise a graduated tubular or rectangular transparentplastic container 378 about 70 cm high with a sealed cap at its top end. This cap may be provided with at least three ports: one port provides a point of connection to the water-manometer line 374; asecond port 380, originally sealed by standard sterile technique, is used thereafter for filling thecontainer 378 withsterile saline solution 382 to the required height within thecontainer 378; and a third port is used for inserting abubbler 384 into thecontainer 378. Thebubbler 384 is a long rigid transparent plastic tube the top open end of which is filled withsterile cotton gauze 386, and the bottom open end of which remains about one cm above the bottom of thecontainer 378.
The height of water orsaline solution 382 in thecontainer 378 determines exactly the negative pressure in the water-manometer line 374, and thevent line 126, provided thevacuum regulator valve 129 is adjusted so that a continuous series of air bubbles 388 appear at the lower end of thebubbler 384 in thesaline solution 382. When thevacuum regulator valve 129 is adjusted such that the negative pressure in thevent line 126 is slightly greater than the height ofliquid 382 in thecontainer 378, air will be sucked through the cotton gauze 386 (or a 0.8 microporous filter), through thebubbler 384, through the water orsaline solution 382, and vented out by the water-manometer line 374 and ventline 126. If the negative pressure in thevent line 126 is less than the height of the water orsaline column 382 in thecontainer 378, air bubbles 388 will not appear in the water orsaline 382. In such a case, thevacuum regulator valve 129 should be readjusted to increase the vacuum until a series ofbubbles 388 are seen in the water orsaline 382.
The amount of negative pressure applied to the emboli filter can be regulated by any other appropriate means. Another alternative means, illustrated in FIG. 8-B, is a piston-like system comprising a hollow cylindricalouter body 420 in which is slideably disposed a flatteneddisk 422 connected to aplunger 424. Thecylindrical body 428 has a forward end with anaperture 416 to which is connected the emboli filtervent line 372. The cylindricalouter body 428 has arearward end 426 through which theplunger 424 passes. A plurality ofsprings 428 are interconnected between thedisk 422 and therearward end 426 of the cylindrical outer body. The circumference of the disk is substantially equal to the circumference of the inner cylindrical body, and fits snugly therewithin. When relaxed, the springs force the disk to therearward end 426 of the cylindricalouter body 420. In operation, once the vacuum source is applying negative pressure to the emboli filter, theplunger 424 is forced toward the forward end of the cylindricalouter body 420, and the springs become distended. As thedisk 422 is urged to the forward end, a first one-way flap valve 430 is closed by the compression building in thechamber 418. Concurrently, a second one-way flap valve 432 opens to allow air to escape thechamber 418. The exuded air is, therefore, not urged into the wound site. Negative pressure is then produced in thechamber 418 of the cylindricalouter body 420. When the pressure in thechamber 418 is less than the atmospheric pressure, thevalve 432 closes and thevalve 430 opens, drawing air from the vent line. Since the wound site is closed, the movement ofpiston 422 away from the inlet port (or the expansion of the chamber 418) creates a negative pressure in the closed wound site, which in turn will induce draining of shed blood from the wound site via thedrainage tubing 310 into the collection bag 390. The magnitude of negative pressure created in the chamber is proportional to the number of springs interconnected between the disk and the cylindrical outer body, the tension achieved by each spring, and the volume of the chamber. The negative pressure is inversely proportional to the friction between thedisk 422 and the inner wall of the cylindricalouter body 420, and the total volume of the closed wound site, plus thedrainage tubing 310 and the volume of the components of the system (emboli filter, membrane filter, bags and tubings).
A filter 376 (i.e., a 0.8 micrometer filter from Millipore Corp., MA.) may be attached to the emboli filtervent line 372 proximate the cylindricalouter body 420 to prevent the transfer of bacteria, viruses, or other harmful agents into the emboli filtervent line 372.
Blood aspirated intosuction tubing 326 is directed through theemboli filter 330. The emboli filter used in this embodiment may be any of those previously described in other embodiments. The blood flows by gravity from the emboli filter 330 into the reservoir 314, and into the blood collection bag 390 through a vertical conduit 392. The vertical conduit 392 should be at least two feet in length to facilitate draining of blood from the reservoir 314 to the blood collection bag 390 by gravity. Such length is also required to overcome the force of negative pressure applied at the embolifilter vent line 372. The bag 390 may contain a precalculated amount of anticoagulant to prevent clotting of blood accumulated in the blood collection bag 390. The vertical conduit 392 is connected to the blood collection bag 390 by a standard connector means 394 (e.g., leur lock). Aclamp 396 may be provided to close the conduit 392 under appropriate conditions described below.
When the blood collection bag 390 becomes almost full with blood 398, the conduit 392 is closed with theclamp 396. Under emergency situations when the patient needs blood immediately, as determined by the physician, the blood collection bag 390 may be easily disconnected from the connector means 394. A fresh sterile blood collection bag may then be attached to the connector means 394 under sterile conditions. The blood collected in the blood collection bag 390 may be reinfused to the patient by attaching a reinfusion line to the infusion port 400 of the blood collection bag 390 and by applying a pressure cuff to the bag. Reinfusion of the blood following filtration through the emboli filter 330 only may be appropriate where immediate reinfusion is necessary to the maintenance of the patient.
Alternatively and preferentially, the blood may be mixed with washing fluid and filtered further. Similar to the embodiment described in FIG. 5, washing fluid may be introduced into the blood in the blood collection bag 390 by securingclamp 396, removingclamp 404 on the tubing interconnected between the blood collection bag 390 and themembrane filter 402, securingclamp 414 on thefiltration line 412, and by manipulating the height of thewashing fluid bag 406 in relation to the blood collection bag 390. That is, thewashing fluid bag 406 should be sequentially raised and lowered above or below the level of the blood collection bag 390 in order to urge washing fluid from the washing fluid line 408 through themembrane filter 402 and into the blood collection bag 390. Alternatively, the washing fluid retainer may be connected to a mechanical device which would sequentially raise and lower thewashing fluid 406.
When the washing fluid has been mixed sufficiently with the blood, theclamp 414 on thefiltration line 412 is opened. The circulation of the blood and washing fluid admixture from the blood collection bag 390 and thewashing fluid bag 406 continues, and as the admixture passes through themembrane filter 402, excess fluid and other matter is filtered off through thefiltration line 412 into thefiltrate receptacle 410. When the amount of fluid in thefiltrate receptacle 410 is roughly equal to the amount of washing fluid originally admixed with the blood, theclamp 414 is replaced on thefiltration line 412 to prevent further filtration. Blood is urged back into the blood collection bag 390 by raising thewashing fluid bag 406 above the level of the blood collection bag 390. When the blood has completely filled the blood collection bag 390 again, theclamp 404 is replaced on the tubing exiting the collection bag, and reinfusion may begin. The blood may be reinfused by attaching a reinfusion line to the port 400 of the blood collection bag 390 and applying a pressure cuff to the bag 390.
The embodiment of FIG. 8-A provides a simple, inexpensive on-line method of purification and drainage of the blood from the emboli filter by providing adequate negative pressure and hydrostatic pressure so that the purified blood can be collected in a conventional blood collection bag for reinfusion purposes.
In these embodiments where washing fluid with anticoagulant is admixed with aspirated blood prior to aspiration into the emboli filter (FIGS. 1, 2, 3, 4, 6, 7 and 12), a specialized suction means 112 may be used where the washing fluid is delivered into the handle of the suction means. Delivery of washing fluid into the suction means has the advantage of providing for more complete admixture, and for less clogging in thesuction tubing 114 due to coagulation of blood in the tubing prior to admixture with the washing fluid. FIG. 13 illustrates a preferred suction means, generally at 270.
Suction tubing 114 is connected to the suction means 270 atconnector point 254, and is connected at its other end (not shown) to the emboli filter. Thewashing fluid line 132 is connected to the suction means 270 atconnector point 256, and is connected at its other end (not shown) to the washing fluid bag. As blood is aspirated through theopen tip 250 of the suction means 270, negative pressure increases to about 120 mm Hg. As a result, washing fluid from the washing fluid bag, which is maintained approximately two feet below the suction means 270, is drawn intowashing fluid line 132. The washing fluid enters into theloop 258 of the suction means 270, and thereby achieves a 180° change in direction of flow. The resulting flow of washing fluid exiting fromloop 258 is parallel to, and in the same direction as, the blood being aspirated through thetip 250. It is only because the aspirated blood and washing fluid are caused to flow in the same direction as a result of this configuration that washing fluid is aspirated in equal proportion to the amount of blood aspirated. The blood and washing fluid are admixed inchamber 252 of the suction means 270, and the admixture is carried to the emboli filter (not shown) viasuction tubing 114.
During surgery, it may occasionally occur that tissues or other matter block thesuction tip 250. If that were to occur, the increased negative pressure would cause washing fluid alone to be aspirated into the emboli filter while no blood is being aspirated. To prevent the aspiration of washing fluid during periods of time when there is no bleeding in the would site (i.e., no blood is being aspirated), and thesuction tip 250 is blocked, anaperture 260 may be provided in the suction means 270 so that air will enter the suction means 270 and reduce the negative pressure. The reduced negative pressure will prevent washing fluid from being aspirated into the suction means 270 and thesuction tubing 114. During normal operation, when thesuction tip 250 is unblocked, the aperture is to be covered by the surgeon's or user's thumb, finger, or hand. Covering the aperture will allow normal increase in the negative pressure to achieve proper aspiration.
The suction means may be made of any suitable material, but is may be preferred to use a transparent material for thesuction tip 250 in order to monitor the occurrence of clogging at the tip.
OPERATION OF THE INVENTION
Referring to FIG. 1, blood is aspirated from theopen wound site 10 by the suction means 12. Aspirated blood flows through thesuction tubing 14 towards the emboli filter 18. Due to the increased negative pressure in thesuction tubing 14, heparinized washing fluid contained in thewashing fluid bag 30 is infused through thewashing fluid line 32 into thesuction tubing 14 at 34 in proportion to the blood flow rate. Thus, the invention provides a mechanism by which washing fluid can be injected into the system in proportion to the aspiration of shed blood without using any pump or control units. A mixture of blood, heparinized washing fluid and some air is drawn into the emboli filter 18 where it is degassified and filtered to remove particles larger than 40 microns. Filtered blood which is free of air emboli is collected in the reservoir 22. Air separated from the blood is vented through thevent line 26 connected to a controlledvacuum source 28.
Blood is drawn from the reservoir 22 by the recirculation pump 36 and circulates through amembrane filter 38, aflow constrictor 40, ahematocrit monitor 42, a recirculation valve 44, and back into the reservoir 22 to be circulated again. It should be noted that thevenous valve 54 remains closed as long as the recirculation valve 44 remains open. Filtrate leaving thefiltrate port 46 is collected in afiltrate receptacle 48. The filtrate typically contains activated coagulation factors, plasma-free hemoglobin, washing fluid, and other impurities which are below the molecular weight cut off of the membrane filter. Recirculation continues until an adequate amount of fluid is removed from the blood by themembrane filter 38 as indicated by thehematocrit monitor 42. When the hematocrit of the blood at the outlet of themembrane filter 38 reaches a set value, the recirculation valve 44 closes and the blood is directed to thereinfusion line 56 through the venous filter 52, with simultaneous opening of thevenous valve 54.
To ensure that no air emboli will be infused with the blood into the patient, and to ensure that no blood having a cellular volume fraction less than the specified value will be reinfused, the invention provides three conditions which must be met in order for thevenous valve 54 to open. These three conditions are: (i) cellular volume fraction of the blood as measured by the conductivity monitor should be at least equal to a set value (e.g., 35%); (ii) venous blood should be free of air emboli as monitored by the ultrasonic detector 58; and (iii) the level of blood in the reservoir 22 should be above the minimum level as monitored by theblood level detector 60.
Should the level of blood in the reservoir 22 fall below the minimum limit as measured by theblood level detector 60, thefiltrate valve 62 located in thefiltration line 45 will close along with thevenous valve 54 to prevent a further fall in the blood level in the reservoir 22.
The invention provides a mechanism by which the filtration rate and the processing of blood can be varied in proportion to the variation in bleeding rate. This is accomplished by varying the speed of the recirculation pump 36 in proportion to the variation in bleeding rate. The recirculation pump 36 may be set to run at a minimum speed corresponding to 100 ml/min when the blood in the reservoir 22 remains below the blood level detector 64. When the bleeding rate increases, the level of blood in the reservoir 22 will rise from the low level detected by theblood level detector 60 to upper level detected by the detector blood level 64. When the blood level rises above the upper level, the speed of the recirculation pump 36 increases gradually until the level of blood falls below the upper level.
Referring to FIG. 3, blood is aspirated from the open wound site by the suction means 112, induced by the controlled vacuum from thevacuum source 128 applied via thevent line 126. Aspirated blood is mixed, in thesuction tubing 114, with the washing fluid from the washingfluid bag 130 in proportion to the suction rate of the blood as described above. Diluted blood enters into the integrated filter, or integrated cascade filter, which comprises anemboli filter 118 andmembrane filter 138. Air emboli are first removed by the emboli filter 118 along with other macroparticles above 40 microns in size. The filtered blood is then collected in thereservoir 122 where it is subjected to membrane filtration by themembrane filter 138. Membrane filtration is induced by thefiltration pump 168 which runs at a constant speed. However, when the level of blood in thereservoir 122 falls below a set limit as detected by theblood level detector 160, or when the cellular volume fraction of blood is above the set limit as measured by theconductivity monitor 142, thefiltration pump 168 will stop.
When the measured cellular volume fraction (hematocrit level) of blood becomes equal to or greater than the set value, theinfusion pump 166 is reactivated to return the processed blood to the patient via thereinfusion line 156; however, the level of blood in thereservoir 122 must remain above the set limit as detected by theblood level detector 160 to avoid air being sucked into the system.
The embodiment of the invention illustrated in FIG. 4 presents a significantly simplified version of the system in which all components are totally disposable, and which operates without the use of any roller pumps, ultrasonic bubble detectors, valves, and other control units. The only equipment required is a controlled vacuum source. The embodiment of the invention is adaptable to an I.V. pole.
When there is bleeding in the open wound site, blood will be aspirated into the emboli filter 118 through thesuction tubing 114. Filtered blood flows out of theemboli filter 118, into thereservoir 122, and through themembrane filter 138 into theblood collection bag 170 by gravity flow. Membrane filtration takes place as the blood passes through themembrane filter 138. Controllednegative pressure 172 may be applied to thefiltrate receptacle 148 by means of avacuum source 172 attached to avacuum line 174 in order to increase filtration rate.
Due to the increased negative pressure in thereservoir 122 as blood is being aspirated, blood is lifted from theblood collection bag 170 to thereservoir 122 through themembrane filter 138. Membrane filtration takes place during this period.
Prior to reinfusion of blood from theblood collection bag 170, the volume of filtrate collected in thefiltrate receptacle 148 should be compared to the volume of washing fluid injected into thesuction tubing 114 to assure that most of the fluid has been removed from the blood. Since both thewashing fluid bag 130 and thefiltrate receptacle 148 are calibrated, the volume of washing fluid consumed and the volume of filtrate collected will be easily determined. If more fluid needs to be removed from the blood, an attending medical person will periodically open and close thesuction tubing 114 at point AA (see FIG. 4) every 3 to 5 minutes in order to maintain a blood flow back and forth between theblood collection bag 170 and thereservoir 122. During this process, further membrane filtration takes place.
When an adequate amount of fluid is removed from the blood and a sufficient amount of blood is collected in theblood collection bag 170, the blood can be reinfused to the patient by gravity flow of the blood throughport 176 of theblood collection bag 170.
The embodiment illustrated in FIG. 5 differs in operation from the embodiment shown in FIG. 4 only by the relative placement of theblood collection bag 170 to the washing fluid retainer means 130 and themembrane filter 138. In this embodiment, aspirated blood enters into the emboli filter 118 and flows by gravity into theblood collection bag 170. Atubing clamp 182 located below the blood collection bag prevents blood from exiting thebag 170. When theblood collection bag 170 is full, the blood may be reinfused to the patient immediately when the medical condition requires. Alternatively, the blood may be reinfused to the patient by attaching a reinfusion line toport 176 and placing a pressure cuff on theblood collection bag 170.
If further purification of the blood is desired or required, thetubing clamp 182 is removed from thetubing 178 interconnected between theblood collection bag 170 and themembrane filter 138, the filtrationline tube clamp 184 is secured, and washing fluid from the washingfluid bag 130 on thefiltration line 145 is allowed to flow through themembrane filter 138 toward theblood collection bag 170. Admixture of blood and washing fluid is thereby accomplished. When the filtrationline tubing clamp 182 is removed, filtration takes place. The filtrate, containing washing fluid, activated coagulation factors, free hemoglobin and other impurities, flows into thefiltrate receptacle 148. As described above, a vacuum force may be applied to thefiltrate receptacle 148 by avacuum source 172 to increase filtration.
As described above, pressure may be intermittently applied at point AA of thesuction tubing 114 to urge recirculation of the blood/washing fluid admixture through themembrane filter 138. When a sufficient amount of fluid has been removed and collected in thefiltrate receptacle 148, the blood may be urged into theblood collection bag 170 or into the washing fluid retainer means 130. The blood may then be reinfused to the patient from theport 176 of theblood collection bag 170 or through theport 133 of thewashing fluid bag 130 by attaching a reinfusion line thereto.
Referring to FIG. 6, when the surgeon wants to aspirate blood from the wound site, thepushbutton 186 located on the handle of the suction means 112 is activated by the surgeon's thumb pressure. As long as thepushbutton 186 remains activated, thetubing clamp 188 onsuction tubing 114 remains open, allowing a mixture of blood and washing fluid to flow into theemboli filter 118. The filtered blood then flows into theblood collection bag 170 through themembrane filter 138.
However, when there is no bleeding, thepushbutton 186 remains inactivated. During this period, thetubing clamp 188 located on thesuction tubing 114 periodically opens and closes thesuction tubing 114 at a predetermined interval (e.g., every one minute). Because of the alternating negative and positive (i.e., atmospheric) pressure in thereservoir 122 due to the closing and opening of theclamp 188, blood is circulated through themembrane filter 138 between thereservoir 122 andblood collection bag 170. Filtration takes place during this process.
Filtration in themembrane filter 138 is achieved by thefiltration pump 168, which may operate at a constant flow rate of 200 ml/min., as long as two conditions are met: (i) the blood level in theblood collection bag 170 remains above the level detected by the ultrasonicblood level detector 158, and (ii) the cellular volume fraction as measured by theconductivity monitor 142 remains below a set value. When these two conditions are not met, thefiltration pump 168 will stop. Similarly, when the blood level remains above the level as detected by theblood level detector 158 and the cellular volume fraction remains above the set value, theblood infusion pump 166 will operate at a predetermined constant flow rate; but theinfusion pump 166 will stop when the two conditions are not met.
The embodiment in FIG. 6 also provides a means for neutralizing any anticoagulant that was mixed with the washing fluid prior to reinfusion of the blood into the patient. The neutralizing substance, such as protamine, is retained in the neutralizer retainer means 190. A specific amount of neutralizer, the concentration of which has been predetermined by the amount and concentration of anticoagulant placed in the washing fluid, is fed into thereinfusion line 156 by theinfusion pump 166 which is designed to have two channels therein.
The embodiments and methods of operation described above are those directed to use during surgery. the embodiments disclosed in FIGS. 7 and 8, however, are those which are used post-surgically to aspirate and filter blood from a closed wound site which has a drainage tube implanted therein.
In FIG. 7, blood from the closed wound site 300 is drawn by thereinfusion pump 334 at a controlled negative pressure through thedrainage tubing 310,suction tubing 326, and emboli filter 330. Thewashing fluid pump 322 infuses washing fluid from the washingfluid bag 320 into thesuction tubing 326. Alternatively, thewashing fluid pump 322 may infuse washing fluid into the closed wound site 300 at a rate proportional to the bleeding rate.
The blood level in the reservoir 314 is always maintained above the limit detected by the ultrasonic air detector 350, which activates theair vent pump 352 to pump out air from the emboli filter 330 only when the blood level falls below the set limit.
Filtered blood free of particulates larger than 40 microns is then subjected to membrane filtration by themembrane filter 336. Whatever fluid is added to the blood will be removed as filtrate by themembrane filter 336. This filtrate typically contains activated coagulation factors and other impurities which are below the molecular weight cut off of the membrane filter. A plasma filter with a molecular weight cut off of a few million daltons or an ultrafilter with a molecular weight cut off of about 40,000 to 400,000 daltons can be chosen as required. The filtered blood is drawn from the integrated cascade filter by thereinfusion pump 334, and is collected in the blood collection bag 338.
The embodiment in FIG. 7 provides a means of exactly balancing the filtration rate to the washing fluid infusion rate, and exactly varying the washing fluid infusion rate in proportion to the bleeding rate in the closed wound site, while maintaining the negative pressure in the closed wound site within safe limits (e.g., below -20 cm of water). This is achieved by employing a three channel roller pump (comprising 322, 344, 334) driven by a single motor and gear unit, and employing apressure control unit 348. The pumping rates of thewashing fluid pump 322 and thefiltrate pump 344 are exactly balanced to each other. Concurrently, the flow rate of thereinfusion pump 334 is kept equal to the bleeding rate by the negativepressure control unit 348. The pressure sensor andcontrol unit 348 associated with the emboli filter 330 increases or decreases the pump speed depending upon whether the negative pressure decreases or increases around a set value (e.g., -20 cm of water). Purified blood may be reinfused to the patient through theport 340 of the blood collection bag 338, either intermittently in batches by gravity flow, or continuously on a real time basis.
The embodiment of FIG. 8-A, which is also used post-surgically, provides a very simple, inexpensive, and disposable system, not dependent upon any capital equipment. Blood flows from the closed wound site via thedrainage tubing 310 into thesuction tubing 326. Blood flows through the one-way valve 370 to theblood inlet port 328 of theemboli filter 330. Aspiration is induced by the negative pressure created by thevacuum line 126, and is approximately controlled by thevacuum regulator valve 129. The negative pressure is accurately controlled by the water-manometer 378. The height ofliquid 382 injected into the water-manometer 378 via the sealedport 380 determines the exact negative pressure in the water-manometer line 374 and ventline 126. Thevacuum regulator valve 129 is adjusted so that a series ofbubbles 388 continuously appear in theliquid column 382. Alternatively, a piston or other means may be used to regulate the negative pressure.
The filtered blood flows down by force of gravity from the reservoir 314 associated with the emboli filter 330 to the blood collection bag 390 via conduit 392 which provides adequate hydrostatic pressure for the blood to flow into the blood collection bag 390. When the bag 390 becomes almost full with filtered blood 398, the conduit 392 is closed with aclamp 396, the blood collection bag 390 is disconnected from the connector means 394, and a fresh sterile blood collection bag is attached to the connector means 394 under sterile conditions. The blood collection bag 390 containing the filtered blood may be suspended from an I.V. pole, and the blood may be reinfused to the patient via the infusion port 400 of the blood collection bag 390. During reinfusion, another conventional emboli filter (e.g., Pall filter) may be used in the reinfusion line to prevent transfer of any blood clots to the patient.
Alternatively, the blood collected in the blood collection bag 390 may be mixed with washing fluid and filtered further. Admixing occurs when theclamp 404 on the tubing interconnected between the blood collection bag 390 and themembrane filter 402 is removed and washing fluid from the washingfluid bag 406 is allowed to flow into the blood collection bag 390. By raising and lowering the height of thewashing fluid bag 406 relative to the blood collection bag 390, the admixture of blood and washing fluid can be made to circulate continuously through themembrane filter 402 which is located therebetween. Filtration occurs whenclamp 414 located on thefiltration line 412 is removed thereby allowing filtrate to be drawn off into thefiltrate receptacle 410. When a sufficient amount of filtrate has been removed, thewashing fluid bag 406 is once again raised above the level of the blood collection bag 390 to cause the blood to flow into the latter.Clamp 404 is then replaced to prevent blood escaping from the blood collection bag 390. Reinfusion may begin as described above.
The simplified embodiment illustrated in FIGS. 10 and 11 is configured to allow immediate transfusion of membrane filtered blood while blood collection continues. It is contemplated that the embodiment of FIG. 10 is attached to an I.V. pole or similar device. While the components of the embodiment function in the same manner as described above, the position of the components in relation to each other allows blood to be infused on a constant, real-time basis. That is, the emboli filtercasing 119 should be kept at least six feet above the ground, and themembrane filter 138 should remain at or about ground level. Because the negative pressure applied by the vacuum source 128 (-120 mm Hg) can only raise blood 5.04 feet, the amount of blood collecting in thereservoir 122, coupled with the length of theconduit 139, allows blood to constantly flow downwardly through theconduit 139. Thus, blood is constantly being filtered through themembrane filter 138 and can be reinfused to the patient from theblood collection bag 170 through theinfusion port 176. While infusion is taking place from theblood collection bag 170, a second blood collection bag is attached to theconnector 198 for further blood collection.
The filtered blood can also be cell-washed by mixing the blood with washing fluid. Washing fluid is contained or placed in theblood collection bag 170. By raising and lowering the height of theblood collection bag 170 relative to themembrane filter 138, blood is forced between theblood collection bag 170 and theconduit 139 which results in admixture of blood in the conduit with washing fluid. During the admixing procedure, aclamp 184 remains on thefiltration line 145 to prevent premature filtration. When admixture is complete, theclamp 184 is removed from thefiltration line 145 and filtration begins. Admixture can take place even while blood collection is occurring.
The embodiment of FIG. 12 presents a further means of collecting and infusing blood on a constant, real-time basis which does not require manipulation of theblood collection bag 170. Rather, theblood collection bag 170 and thefiltrate receptacle 148 are connected to thesame vacuum source 128 to which the emboli filtercasing 119 is attached. Negative pressure applied to theblood collection bag 170 enhances blood collection, and negative pressure applied to thefiltrate receptacle 148 enhances filtration. Because thefiltrate receptacle 148 is attached to thesame vacuum source 128 as the emboli filtercasing 119, when negative pressure increases with blood aspiration, filtration correspondingly increases.
Aspirated blood is admixed with washing fluid aspirated from the washingfluid bag 130 insuction tubing 114. Admixed blood/washing fluid is filtered through theemboli filter 118, and is then carried through theconduit 139. Theconduit 139 is fitted with bubble traps 232, 234 to allow the venting off of any residual bubbles which, when trapped in the blood column in theconduit 139, decrease or prevent the flow of blood in the column.
Though the blood may be filtered through themembrane filter 138 in a single pass, the blood may be further filtered by causing blood collected in theblood collection bag 170 to flow into thereservoir bag 224 associated with theconduit 139. Blood may be made to flow from theblood collection bag 170 into thereservoir bag 224 by sequentially producing negative pressure and positive (atmospheric) pressure in theblood collection bag 170. Manipulation of negative and positive pressure in theblood collection bag 170 is accomplished by manipulating the two-way valve 212 associated with theblood collection bag 170; the two-way valve 212 operates to either allow vacuum suction to be applied to theblood collection bag 170, or to introduce atmospheric pressure into theblood collection bag 170. As alternating negative and positive pressure is applied to theblood collection bag 170, blood is caused to circulate between the blood circulation bag and thereservoir bag 224. Filtration occurs with every pass through themembrane filter 138. Two blood collection bags are provided so that one may become full, and reinfusion can take place from thatblood collection bag 170 while the other blood collection bag 214 (or stand-by bag) continues to fill with filtered blood. Infusion from the blood collection bag takes place when an infusion line is attached to theinfusion port 176 of theblood collection bag 170, theclamp 216 attached to thesecond conduit 141 below theblood collection bag 170 is secured in the closed position, and atmospheric pressure is introduced into the bag by engaging the two-way valve 212 in the open position. Infusion then takes place by gravity flow. At the same time, theclamp 218 on thesecond conduit 141 leading to the stand-byblood collection bag 214 is opened to allow blood to collect therein. Negative pressure is applied to theblood collection bag 214 by engaging the two-way valve 220 to open to thevent line 210 of thevacuum source 128.
The various embodiments of the invention provide membrane filtration systems for both intraoperative and post-surgical applications, which operate continuously on-line, on a real time basis, providing washing fluid in proportion to bleeding rate, filtration to remove particulates larger than 40 micron, and membrane filtration to remove washing fluid, and other impurities which are below a desired molecular size. Most importantly, the present invention provides to the patient, in some embodiments, his/her own purified blood at the required hematocrit value free of air emboli at the same rate at which it is lost from the wound site.
The embodiments shown in the figures, along with the descriptions thereof, are by way of illustration and are not intended to limit the possible configurations of the invention or to limit the scope of the invention as claimed below.

Claims (64)

What is claimed is:
1. An apparatus for filtering autologous blood taken from a patient for reinfusion to the patient comprising:
suction means for aspirating blood from a wound site;
first conduit means for conducting said aspirated blood from said suction means;
washing fluid retainer means for retaining washing fluid for admixing with said aspirated blood;
second conduit means interconnected between said washing fluid retainer means and said first conduit for conducting washing fluid therebetween;
first filter means for removing emboli and large particulates from said aspirated blood, said first filter means being connected to said first conduit means;
filter casing means for enclosing said first filter means therein, said filter casing having vacuum connector means associated therewith for attaching a source of vacuum;
reservoir means associated with said filter casing means for collecting filtered blood from said first filter means;
second filter means for filtering excess fluids and impurities from said blood;
third conduit means interconnected between said reservoir means and said second filter means for conducting blood therebetween;
blood collection means for collecting filtered blood;
fourth conduit means interconnected between said second filter and said blood collection means for conducting filtered blood therebetween;
filtrate container means for containing said excess fluids and impurities filtered from said blood by said second filter means;
fifth conduit means interconnected between said second filter means and said filtrate container means for conducting filtrate therethrough; and
reinfusion means associated with said blood collection means for reinfusing purified blood to the patient.
2. The apparatus of claim 1 wherein said washing fluid retainer means is positioned below said suction means.
3. The apparatus of claim 2 wherein said first filter means is positioned from about two feet to about five feet above the relative height of said suction means.
4. The apparatus of claim 3 wherein said first filter means is positioned relative to said second filter means to enable movement of blood to the latter by gravity.
5. The apparatus of claim 4 wherein said blood collection means is positioned at a height above the relative height of said second filter means.
6. The apparatus of claim 5 wherein said filtrate container means has vacuum connector means associated therewith.
7. The apparatus of claim 6 further comprising adjustable clamp means associated with said first conduit for closing off said first conduit.
8. The apparatus of claim 6 wherein said blood collection means comprises a plurality of non-collapsible containers, each container having associated therewith a vacuum connector means for attaching a source of vacuum.
9. The apparatus of claim 8 wherein said fourth conduit is divided into separate branches, each said separate branch of said fourth conduit being attachable to a said non-collapsible container.
10. The apparatus of claim 9 further comprising vacuum line means associated with each said vacuum connector means of each said non-collapsible container and further associated with said vacuum connector means of said filter casing, said vacuum line being attachable to a vacuum source.
11. The apparatus of claim 10 further comprising vacuum control means associated with said vacuum line to control the amount of pressure applied to each said non-collapsible container by the vacuum source.
12. The apparatus of claim 11 further comprising filter means attached to said vacuum line associated with each said non-collapsible container for filtering and preventing unwanted particles from entering said non-collapsible containers through said vacuum line.
13. The apparatus of claim 12 wherein said vacuum line is also connected to said vacuum connector means of said filtrate container.
14. The apparatus of claim 13 further comprising air venting means for venting off entrapped air bubbles from the blood, said air venting means being interconnected between said third conduit and said filter casing means.
15. The apparatus of claim 14 further comprising auxiliary blood collection means connected to said third conduit means for collecting blood therein, said auxiliary blood collection means having port means for conducting fluids therethrough.
16. The apparatus of claim 5 further comprising first blood level detector means associated with said blood collection means for detecting the level of blood in said blood collection means.
17. The apparatus of claim 16 further comprising second blood component level detector means associated with said reinfusion means for measuring the level of blood components in said blood prior to reinfusion.
18. The apparatus of claim 17 further comprising anticoagulant neutralizer container means connected to said reinfusion means for retaining anticoagulant neutralizer.
19. The apparatus of claim 18 further comprising first pump means connected to said reinfusion means for pumping blood from said blood collection means to said patient.
20. The apparatus of claim 19 further comprising second pump means connected to said fifth conduit for urging said filtrate from said second filter means.
21. The apparatus of claim 20 further comprising control means in electro-mechanical communication with said adjustable clamp means associated with said first conduit means for actuating said clamp means.
22. The apparatus of claim 1 wherein said first filter further comprises porous material having a pore size of about 40 microns and having an upper end and a lower end, said lower end being covered with hydrophilic fabric and said upper end being covered with hydrophobic fabric, and said porous material being contacted with an antifoam agent.
23. The apparatus of claim 1 wherein said second filter comprises a porous membrane having a pore size from about 40,000 daltons to about 0.4 microns.
24. The apparatus of claim 23 wherein said pore size of said porous membrane is about 100,000 daltons.
25. The apparatus of claim 1 wherein said suction means further comprises:
handle means for grasping;
first duct means for passage of blood therethrough, said first duct means having a first end defining a tip and a second end for connection to said first conduit means;
second duct means for passage of washing fluid therethrough, said second duct having a first opening in communication with said second conduit means and a second opening in communication with said first duct means such that said first duct means and said second duct means are substantially parallel and the movement of said blood through said fist duct means and the movement of said washing fluid in said second duct means is in the same direction.
26. An apparatus for filtering autologous blood taken from a patient for reinfusion to the patient comprising:
suction means for aspirating blood from a wound site;
first conduit means for conducting said aspirated blood from said suction means;
first filter means for removing emboli and large particulates from said aspirated blood, said first filter means being connected to said first conduit means;
filter casing means for enclosing said first filter means therein, said filter casing having vacuum connector means associated therewith for attaching a source of vacuum;
reservoir means associated with said filter casing means for collecting filtered blood from said first filter means;
second filter means for filtering excess fluids and impurities from said blood;
second conduit means interconnected between said reservoir means and said second filter means for conducting blood therebetween;
blood collection means for collecting filtered blood;
third conduit means interconnected between said second filter and said blood collection means for conducting filtered blood therebetween;
filtrate container means for containing said excess fluids and impurities filtered from said blood by said second filter means;
fourth conduit means interconnected between said second filter means and said filtrate container means for conducting filtrate therethrough;
first adjustable clamp means associated with said fourth conduit means for preventing flow of filtrate therethrough; and
reinfusion means associated with said blood collection means for reinfusing purified blood to the patient.
27. The apparatus of claim 26 wherein said third conduit further comprises separate branches, each branch having connector means for attaching blood collection means thereto.
28. The apparatus of claim 27 wherein each said blood collection means has a port means for passage of fluids therethrough.
29. The apparatus of claim 26 further comprising auxiliary blood retainer means connected to said second conduit means for retaining blood conducted through said second conduit from said reservoir, and further comprising second adjustable clamp means associated with said second conduit means between said auxiliary blood retainer means and said second filter means for preventing fluid from passing therebetween.
30. The apparatus of claim 29 wherein said auxiliary blood retainer means has port means for passage of fluid therethrough.
31. The apparatus of claim 30 wherein said blood collection means contains washing fluid therein for mixing with said aspirated blood.
32. The apparatus of claim 31 wherein said suction means is positioned from about two feet to about five feet below the relative height of said first filter means, wherein said first filter means is at least six feet in height above said second filter means, and wherein said second conduit means is at least six feet in length.
33. The apparatus of claim 32 further comprising vacuum regulator means in communication with said first filter means for regulating the amount of negative pressure applied thereto.
34. The apparatus of claim 33 wherein said vacuum regulator means is a water manometer.
35. The apparatus of claim 34 further comprising bifurcated vacuum line means for attachment to a vacuum source, one end of said bifurcated vacuum line means being connected to said vacuum connector means of said filter casing means and the other end of said bifurcated vacuum line means being attached to said water manometer.
36. The apparatus of claim 35 wherein said bifurcated vacuum line has first valve means connected thereto, in proximity to said filter casing means, for preventing flow of liquid into said vacuum line means, and further comprising vacuum monitor means associated with said bifurcated vacuum line means for monitoring the pressure supplied by said vacuum source.
37. The apparatus of claim 36 further comprising valve means attached to said first conduit means for preventing backflow of matter therethrough.
38. The apparatus of claim 37 further comprising third adjustable clamp means connected to said second conduit means between said first filter means and said auxiliary blood retainer means for preventing passage of blood therethrough.
39. The apparatus of claim 33 wherein said vacuum regulator means is a piston-type regulator.
40. The apparatus of claim 32 further comprising vacuum connector means associated with said filtrate container means for attachment of a source of vacuum.
41. The apparatus of claim 26 wherein said first filter further comprises porous material having a pore size of about 40 microns and having an upper end and a lower end, said lower end being covered with hydrophilic fabric and said upper end being covered with hydrophilic fabric, and said porous material being contacted with an antifoam agent.
42. The apparatus of claim 26 wherein said second filter comprises a porous membrane having a pore size from about 40,000 daltons to about 0.4 microns.
43. The apparatus of claim 42 wherein said pore size of said porous membrane is about 100,000 daltons.
44. An apparatus for filtering autologous blood taken from a patient for reinfusion to the patient comprising:
suction means for aspirating blood from a wound site;
first conduit means for conducting said aspirated blood from said suction means;
washing fluid retainer means for retaining washing fluid for admixing with said aspirated blood;
second conduit means interconnected between said washing fluid retainer means and said first conduit for conducting washing fluid therebetween;
first filter means for removing emboli and large particulates from said aspirated blood, said first filter means being connected to said first conduit means;
filter casing means for enclosing said first filter means therein, said filter casing having vacuum connector means associated therewith for attaching a source of vacuum;
reservoir means associated with said filter casing means for collecting filtered blood from said first filter means;
second filter means for filtering excess fluids and impurities from said blood, said second filter being in communication with said filter casing means;
filtrate container means for containing said excess fluids and impurities filtered from said blood by said second filter means;
third conduit means interconnected between said second filter means and said filtrate container means for conducting filtrate therethrough; and
fourth conduit means in communication with said reservoir means for conducting filtered blood therethrough for reinfusion.
45. The apparatus of claim 44 wherein said first filter means and said second filter means are conjoined into said filter casing means, and further comprising vacuum connector means associated with said filter casing means for attaching a source of vacuum.
46. The apparatus of claim 45 further comprising first pump means associated with said third conduit means for urging said filtrate therethrough, second pump means associated with said fourth conduit means for urging filtered blood therethrough, and blood level detector means connected to said reservoir means for detecting the level of blood therein.
47. The apparatus of claim 46 further comprising blood component detector means connected to said fourth conduit means for detecting blood component levels in blood passing therethrough.
48. The apparatus of claim 46 further comprising third pump means associated with said second conduit for urging washing fluid therethrough.
49. The apparatus of claim 48 wherein said first pump means, said second pump means, and said third pump means are in electromechanical communication with each other.
50. The apparatus of claim 49 further comprising vent pump means associated with said filter casing means for venting air from said filter casing means and first filter means, and further comprising pressure regulator means connected to said filter casing means for regulating pressure thereto.
51. The apparatus of claim 44 further comprising fifth conduit means interconnected between said reservoir means and said second filter means for conducting blood therebetween, and further comprising recirculation pump means associated with said fifth conduit for urging blood therethrough.
52. The apparatus of claim 51 further comprising sixth conduit means interconnected between said second filter means and said reservoir means for conducting blood therethrough, said sixth conduit means being in communication with said fourth conduit means.
53. The apparatus of claim 52 further comprising blood level detector means associated with said reservoir means for measuring high and low levels of blood in said reservoir means.
54. The apparatus of claim 53 further comprising flow constriction means associated with said second filter means for providing transmembrane pressure in said second filter.
55. The apparatus of claim 54 further comprising blood component level detector means connected to said sixth conduit means for measuring the level of blood components in said blood.
56. The apparatus of claim 55 further comprising first valve means connected to said fourth conduit means and said sixth conduit means for alternately directing blood through said sixth conduit means and said fourth conduit means.
57. The apparatus of claim 56 further comprising second valve means connected to said third conduit means for opening and closing said conduit means.
58. The apparatus of claim 57 wherein said first valve means, said second valve means, said recirculation pump means and said blood component level detector means are in electromechanical communication with each other.
59. The apparatus of claim 58 further comprising third filter means connected to said fourth conduit means for filtering emboli and residual impurities from the blood prior to infusion, said filter having blood level detector means connected thereto for measuring the level of blood in said third filter means, and further comprising third valve means connected to said fourth conduit means for closing said fourth conduit, said third valve means being in electromechanical communication with said blood level detector means of said third filter means, said blood level detector means of said reservoir means, and said blood component level detector means.
60. The apparatus of claim 44 wherein said suction means further comprises:
handle means for grasping;
first duct means for passage of blood therethrough, said first duct means having a first end defining a tip and a second end for connection to said first conduit means;
second duct means for passage of washing fluid therethrough, said second duct having a first opening in communication with said second conduit means and a second opening in communication with said first duct means such that said first duct means and said second duct means are substantially parallel and the movement of said blood through said fist duct means and the movement of said washing fluid in said second duct means is in the same direction.
61. A method of recycling autologous blood for reinfusion into a patient comprising:
aspirating an amount of blood from a wound site under vacuum pressure;
admixing said blood with an amount of washing fluid approximately proportional to that of said blood;
introducing said admixture of approximately proportional amounts of blood and washing fluid into a first emboli filter under vacuum pressure;
filtering said admixture of blood and washing fluid through said emboli filter to remove air and large particles;
filtering said admixture through a membrane filter to remove impurities and excess fluid; and
reinfusing said filtered blood into said patient.
62. The method according to claim 61 further comprising monitoring said blood for volume of cellular components in said blood after filtering said blood through said membrane filter.
63. The method according to claim 62 further comprising recirculating said blood through said membrane filter and said emboli filter prior to reinfusing said blood into said patient until a desired amount of excess fluid and impurities have been removed, and a desired volume of blood cellular components remain in said blood.
64. The method according to claim 63 further comprising filtering said blood through a second emboli filter prior to reinfusing said blood into said patient to remove any air emboli and impurities therefrom.
US07/525,5361990-03-071990-05-18Autologous blood recovery membrane system and methodExpired - Fee RelatedUS5055198A (en)

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US07/525,536US5055198A (en)1990-03-071990-05-18Autologous blood recovery membrane system and method
DE69125931TDE69125931T2 (en)1990-03-071991-03-06 AUTOLOGICAL BLOOD RECOVERY SYSTEM
EP91906022AEP0518975B1 (en)1990-03-071991-03-06Autologous blood recovery system
JP3506174AJP3012689B2 (en)1990-03-071991-03-06 Autologous blood collection membrane system and method
PCT/US1991/001530WO1991013677A1 (en)1990-03-071991-03-06Autologous blood recovery membrane system and method
US07/730,705US5215519A (en)1990-03-071991-07-16Autotransfusion membrane system with means for providing reverse filtration

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Cited By (228)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
WO1993001858A1 (en)*1991-07-161993-02-04Asahi Medical Co., LtdAutotransfusion membrane system
US5234403A (en)*1990-05-251993-08-10Sumitomo Bakelite Co., Ltd.Blood collecting apparatus
US5330425A (en)*1992-04-301994-07-19Utterberg David SBlow molded venous drip chamber for hemodialysis
US5378227A (en)*1992-08-111995-01-03Cobe Laboratories, Inc.Biological/pharmaceutical method and apparatus for collecting and mixing fluids
EP0636379A1 (en)*1993-06-281995-02-01C.R. Bard, Inc.Disposable blood washing and apheresis device
US5407425A (en)*1989-12-291995-04-18Werner; MargritSystem for the collecting and retransfusion of autologous blood
US5441482A (en)*1994-05-111995-08-15The Regents Of The University Of MinnesotaJet driven surgical suction device and method of using
US5484469A (en)*1992-02-141996-01-16Hoeganaes CorporationMethod of making a sintered metal component and metal powder compositions therefor
US5656027A (en)*1995-06-061997-08-12Cobe Laboratories, Inc.Surgical fluid suction accumulator and volume measurement device
US5674394A (en)*1995-03-241997-10-07Johnson & Johnson Medical, Inc.Single use system for preparation of autologous plasma
US5743894A (en)*1995-06-071998-04-28Sherwood Medical CompanySpike port with integrated two way valve access
US5770073A (en)*1996-03-151998-06-23Minntech CorporationCombined cardiotomy and venous reservoir
WO1998029149A1 (en)*1997-01-031998-07-09Shettigar U RamakrishnaIntraoperative blood salvaging system and method
US5795159A (en)*1996-02-021998-08-18The United States Of America As Represented By The Secretary Of The NavyMercury removal method and apparatus
US5876611A (en)*1997-06-161999-03-02Shettigar; U. RamakrishnaIntraoperative blood salvaging system and method
US5925025A (en)*1996-06-051999-07-20Tyco Group S.A.R.L.Filtration valve cap with reflux clearing feature and related method of use thereof
US5931821A (en)*1996-03-051999-08-03Tyco Group S.A.R.L.Chest drainage unit with controlled automatic excess negativity relief feature
US5971948A (en)*1995-12-131999-10-26Haemonetics CorporationApparatus for collection, washing, and reinfusion of shed blood
US5989438A (en)*1997-12-121999-11-23Baxter International Inc.Active blood filter and method for active blood filtration
US5993406A (en)*1997-05-141999-11-30Cedars-Sinai Medical CenterArtificial gut
US6017493A (en)*1997-09-262000-01-25Baxter International Inc.Vacuum-assisted venous drainage reservoir for CPB systems
US6099493A (en)*1997-05-062000-08-08Sherwood Services, AgContinuous autotransfusion filtration system
US6213334B1 (en)1996-09-052001-04-10Baxter International IncFlexible, three-dimensional containers and methods for making them
US6217544B1 (en)1997-05-302001-04-17Sherwood Services, AgFiltration valve cap with reflux clearing feature and related method of use thereof
US6232115B1 (en)1996-06-252001-05-15Thermogenesis Corp.Freezing and thawing bag, mold, apparatus and method
US6251295B1 (en)*1998-01-082001-06-26Nexell Therapeutics Inc.Method for recirculation washing of blood cells
US6251291B1 (en)1998-12-282001-06-26Tranfusion Technologies CorporationReservoir-and-filter system and method of use
JP3186770B2 (en)1991-11-152001-07-11デカ・プロダクツ・リミテッド・パートナーシップ Intravenous injection device having air removal means
US6302860B1 (en)*1999-02-172001-10-16Medtronic, Inc.Venous filter for assisted venous return
US20020031836A1 (en)*2000-09-112002-03-14Feldstein Mark J.Fluidics system
US6361642B1 (en)1997-12-022002-03-26Baxter International Inc.Heat and pressure-formed flexible containers
US6367634B1 (en)1993-12-222002-04-09Baxter International Inc.Blood collection systems including an integral, flexible filter
US6422397B1 (en)1993-12-222002-07-23Baxter International, Inc.Blood collection systems including an integral, flexible filter
US20020099401A1 (en)*1990-06-282002-07-25Bonutti Petel M.Apparatus and method for tissue removal
US20020096467A1 (en)*2000-12-012002-07-25Jean-Marc CappiaChemical process system with multi-functional barrier filter
US6547775B1 (en)1998-10-222003-04-15Medtronic, Inc.Atraumatic blood suction system
US6555360B1 (en)*1998-03-302003-04-29Friedrich SriencFlow injection flow cytometry system for on-line monitoring of biroreactors and method for monitoring
US20030130744A1 (en)*1991-08-122003-07-10Bonutti Peter M.Tissue cage
US6601710B2 (en)1999-04-202003-08-05Baxter International Inc.Filter assembly having a flexible housing
US6632192B2 (en)*2001-03-052003-10-14Transvivo, Inc.Apparatus and method for selective reduction of segmental intracellular and extracellular edema
WO2003090839A1 (en)*2002-04-242003-11-06Interpore OrthopaedicsBlood separation and concentration system
US20030209479A1 (en)*2000-07-102003-11-13Lynn Daniel RBlood filters, blood collection and processing systems, and methods therefore
EP1374929A1 (en)*2002-06-252004-01-02Jostra AGApparatus for elimination of gas bubbles
US20040009097A1 (en)*2001-02-092004-01-15Cardiovention, Inc.Integrated blood handling system having active gas removal system and methods of use
US20040019310A1 (en)*2002-07-292004-01-29Michael HogendijkBlood aspiration system and methods of use
US6695803B1 (en)1998-10-162004-02-24Mission Medical, Inc.Blood processing system
US20040089050A1 (en)*2001-03-202004-05-13Daw Derek J.Bubble detector and method of evaluation or calibration thereof
US20040147865A1 (en)*1994-10-132004-07-29Cianci James P.System and method for processing blood
US6773670B2 (en)2001-02-092004-08-10Cardiovention, Inc. C/O The Brenner Group, Inc.Blood filter having a sensor for active gas removal and methods of use
US20040184953A1 (en)*2003-03-172004-09-23Litzie A. KennethExtracorporeal blood handling system with automatic flow control and methods of use
US20040195178A1 (en)*2003-01-142004-10-07Carpenter Walter L.Extracorporeal blood circuit priming system and method
US20040197223A1 (en)*2003-01-142004-10-07Olsen Robert W.Active air removal system operating modes of an extracorporeal blood circuit
US6808675B1 (en)1996-06-252004-10-26Thermogenesis Corp.Freezing and thawing bag, mold, apparatus and method
US20040214314A1 (en)*2001-11-022004-10-28Friedrich SriencHigh throughput bioreactor
US20040220509A1 (en)*2003-01-142004-11-04Olsen Robert W.Active air removal from an extracorporeal blood circuit
US20040238444A1 (en)*2003-05-272004-12-02Michael RagusaContinuous blood filtration and method of use
US20050063860A1 (en)*2003-01-142005-03-24Carpenter Walter L.Disposable, integrated, extracorporeal blood circuit
US20050101261A1 (en)*2003-11-102005-05-12Ronald LachmanBluetooth interface between cellular and wired telephone networks
US6918887B1 (en)1999-02-172005-07-19Medtronic, Inc.Venous filter for assisted venous return
US6990982B1 (en)1990-06-282006-01-31Bonutti Ip, LlcMethod for harvesting and processing cells from tissue fragments
WO2006101447A1 (en)*2005-03-242006-09-28Sifr 2000 AbControl of bubble formation in extracorporeal circulation
US20060270974A1 (en)*2005-05-162006-11-30Kerberos Proximal Solutions, Inc.Methods and systems for filtering aspirated materials
US20070066945A1 (en)*2003-10-282007-03-22Martin Robin PWound cleansing apparatus with scaffold
US7204958B2 (en)2003-01-142007-04-17Medtronic, Inc.Extracorporeal blood circuit air removal system and method
US20070129707A1 (en)*2003-10-282007-06-07Blott Patrick LWound cleansing apparatus with heat
US20070167926A1 (en)*2003-10-282007-07-19Blott Patrick LWound cleansing apparatus in-situ
US20080234641A1 (en)*2007-02-092008-09-25Christopher Brian LockeSystem and method for managing reduced pressure at a tissue site
US20090069759A1 (en)*2004-04-272009-03-12Smith & Nephew , Plc.Apparatus for cleansing wounds with means for supply of thermal energy to the therapy fluid
US20090101023A1 (en)*2006-04-032009-04-23Mermaid Co., Ltd.Fryer
US20090175762A1 (en)*2008-01-082009-07-09Terumo Kabushiki KaishaOxygenator unit and oxygenator apparatus
US20090204084A1 (en)*2005-09-152009-08-13Patrick Lewis BlottApparatus
US7613491B2 (en)2002-05-222009-11-03Dexcom, Inc.Silicone based membranes for use in implantable glucose sensors
US7615007B2 (en)2006-10-042009-11-10Dexcom, Inc.Analyte sensor
US20090292263A1 (en)*2008-05-212009-11-26Tyco Healthcare Group, LpWound therapy system with portable container apparatus
US20090314724A1 (en)*2006-09-082009-12-24Arno Pieter NierichBlood recuperation device and method
US7640048B2 (en)2004-07-132009-12-29Dexcom, Inc.Analyte sensor
US20100030151A1 (en)*2008-07-302010-02-04Claudia KirschDebubbler
US20100042059A1 (en)*2008-08-082010-02-18Benjamin Andrew PrattReduced-pressure treatment systems with reservoir control
US20100133175A1 (en)*2008-10-202010-06-03Photonic Biosystems, Inc.Filtered Assay Device and Method
US7753894B2 (en)2004-04-272010-07-13Smith & Nephew PlcWound cleansing apparatus with stress
US7762976B2 (en)2004-01-202010-07-27Sorin Group Deutschland GmbhAutomatic air removal system
US20100211031A1 (en)*2007-07-022010-08-19Edward HartwellWound treatment apparatus with exudate volume reduction by heat
US7783333B2 (en)2004-07-132010-08-24Dexcom, Inc.Transcutaneous medical device with variable stiffness
US20100270222A1 (en)*2009-04-232010-10-28Fresenius Medical Care Deutschland GmbhDevice and external functional means and treatment apparatus for the treatment of medical fluids
US20100298792A1 (en)*2008-01-082010-11-25Bluesky Medical Group Inc.Sustained variable negative pressure wound treatment and method of controlling same
US7885697B2 (en)2004-07-132011-02-08Dexcom, Inc.Transcutaneous analyte sensor
US20110068061A1 (en)*2009-09-222011-03-24Haemonetics CorporationIntegrated Measurement System For Use with Surgical Fluid Salvage Containers
US7927319B2 (en)2007-02-202011-04-19Kci Licensing, Inc.System and method for distinguishing leaks from a disengaged canister condition in a reduced pressure treatment system
US20110139723A1 (en)*2009-12-112011-06-16General Electric CompanyDisposable fluid path systems and methods for processing complex biological materials
US8118794B2 (en)2002-09-032012-02-21Bluesky Medical Group, Inc.Reduced pressure treatment system
US8173018B2 (en)2010-08-252012-05-08Dow Global Technologies LlcFluid filter module including sealed boss
US20120130299A1 (en)*2009-05-292012-05-24Sorin Group Deutschland GmbhDevice for Establishing the Venous Inflow to a Blood Reservoir of an Extracorporeal Blood Circulation System
US8257327B2 (en)2003-10-282012-09-04Smith & Nephew PlcWound cleansing apparatus with actives
US8261919B2 (en)2010-08-252012-09-11Dow Global Technologies LlcFluid filter module including handle
US8275438B2 (en)2006-10-042012-09-25Dexcom, Inc.Analyte sensor
US8282611B2 (en)2004-04-052012-10-09Bluesky Medical Group, Inc.Reduced pressure wound treatment system
US8287453B2 (en)2003-12-052012-10-16Dexcom, Inc.Analyte sensor
US8290559B2 (en)2007-12-172012-10-16Dexcom, Inc.Systems and methods for processing sensor data
US20120271254A1 (en)*2011-02-222012-10-25Schafer Mark ECanister for autologous fat transfer
US8298142B2 (en)2006-10-042012-10-30Dexcom, Inc.Analyte sensor
US8328776B2 (en)2006-09-192012-12-11Kci Licensing, Inc.Reduced pressure treatment system having blockage clearing and dual-zone pressure protection capabilities
US8364231B2 (en)2006-10-042013-01-29Dexcom, Inc.Analyte sensor
US8364229B2 (en)2003-07-252013-01-29Dexcom, Inc.Analyte sensors having a signal-to-noise ratio substantially unaffected by non-constant noise
US8364230B2 (en)2006-10-042013-01-29Dexcom, Inc.Analyte sensor
US8366690B2 (en)2006-09-192013-02-05Kci Licensing, Inc.System and method for determining a fill status of a canister of fluid in a reduced pressure treatment system
US8396528B2 (en)2008-03-252013-03-12Dexcom, Inc.Analyte sensor
US8398614B2 (en)2002-10-282013-03-19Smith & Nephew PlcApparatus for aspirating, irrigating and cleansing wounds
US8417312B2 (en)2007-10-252013-04-09Dexcom, Inc.Systems and methods for processing sensor data
US20130092630A1 (en)*2011-03-112013-04-18Fenwal, Inc.Disposable Fluid Circuits And Methods For Cell Washing With On-Line Dilution Of Cell Feed
US8425417B2 (en)2003-12-052013-04-23Dexcom, Inc.Integrated device for continuous in vivo analyte detection and simultaneous control of an infusion device
US8425416B2 (en)2006-10-042013-04-23Dexcom, Inc.Analyte sensor
US8447376B2 (en)2006-10-042013-05-21Dexcom, Inc.Analyte sensor
US8449509B2 (en)2004-04-052013-05-28Bluesky Medical Group IncorporatedFlexible reduced pressure treatment appliance
US8449464B2 (en)2006-10-042013-05-28Dexcom, Inc.Analyte sensor
US8460255B2 (en)2006-05-112013-06-11Kalypto Medical, Inc.Device and method for wound therapy
US8478377B2 (en)2006-10-042013-07-02Dexcom, Inc.Analyte sensor
US8529548B2 (en)2004-04-272013-09-10Smith & Nephew PlcWound treatment apparatus and method
US8562558B2 (en)2007-06-082013-10-22Dexcom, Inc.Integrated medicament delivery device for use with continuous analyte sensor
US8562528B2 (en)2006-10-042013-10-22Dexcom, Inc.Analyte sensor
CN103405820A (en)*2013-08-262013-11-27佛山市博新生物科技有限公司Special line for blood perfusion hemodiasysis treatment and operation method thereof
US8626257B2 (en)2003-08-012014-01-07Dexcom, Inc.Analyte sensor
US20140050615A1 (en)*2012-08-152014-02-20Cyclone Medtech, Inc.Systems and methods for salvaging red blood cells for autotransfusion
US8663198B2 (en)2009-04-172014-03-04Kalypto Medical, Inc.Negative pressure wound therapy device
US8715256B2 (en)2007-11-212014-05-06Smith & Nephew PlcVacuum assisted wound dressing
US8758313B2 (en)2003-10-282014-06-24Smith & Nephew PlcApparatus and method for wound cleansing with actives
US8764732B2 (en)2007-11-212014-07-01Smith & Nephew PlcWound dressing
US8795243B2 (en)2004-05-212014-08-05Bluesky Medical Group IncorporatedFlexible reduced pressure treatment appliance
US8808274B2 (en)2007-11-212014-08-19Smith & Nephew PlcWound dressing
US8829263B2 (en)2005-09-072014-09-09Smith & Nephew, Inc.Self contained wound dressing with micropump
CN104096275A (en)*2014-07-182014-10-15杨国锋Post-operation auto-blood recycling device
US8886273B2 (en)2003-08-012014-11-11Dexcom, Inc.Analyte sensor
US8945074B2 (en)2011-05-242015-02-03Kalypto Medical, Inc.Device with controller and pump modules for providing negative pressure for wound therapy
US8945376B1 (en)2013-08-022015-02-03All Cell Recovery LLCSystems, methods, and apparatus for resuspending cells in solution
US9044579B2 (en)2005-04-272015-06-02Smith & Nephew PlcWound treatment apparatus and method
US9044569B2 (en)2004-04-282015-06-02Smith & Nephew PlcWound dressing apparatus and method of use
US9058634B2 (en)2011-05-242015-06-16Kalypto Medical, Inc.Method for providing a negative pressure wound therapy pump device
US9061095B2 (en)2010-04-272015-06-23Smith & Nephew PlcWound dressing and method of use
US9067003B2 (en)2011-05-262015-06-30Kalypto Medical, Inc.Method for providing negative pressure to a negative pressure wound therapy bandage
US20150209565A1 (en)*2012-08-292015-07-30Euromi, S.AApparatus for extracting and re-injecting adipose tissue
US9135402B2 (en)2007-12-172015-09-15Dexcom, Inc.Systems and methods for processing sensor data
CN105408467A (en)*2013-07-232016-03-16株式会社钟化Method for producing cell concentrate, and cell suspension treatment system
US9289546B2 (en)2012-08-162016-03-22Dirk Jerome EricksonExsanguination preventing device
WO2016057664A1 (en)2014-10-072016-04-14Haemonetics CorporationSystem and method for washing shed blood
US9327066B2 (en)2013-03-132016-05-03Keith SamolykCPB system with dual function blood reservoir
CN105536086A (en)*2016-02-232016-05-04南京医科大学第一附属医院Multifunctional ECMO circulating pipeline and method for performing extracorporeal membrane oxygenation by utilizing multifunctional ECMO circulating pipeline
US9446354B2 (en)2010-08-252016-09-20Repligen CorporationDevice, system and process for modification or concentration of cell-depleted fluid
US9452021B2 (en)2013-08-022016-09-27All Cell Recovery LLCSystems, methods, and apparatus for resuspending cells from surgical laundry
US9452253B2 (en)*2013-03-132016-09-27Keith SamolykCPB system with fluid volume control
US9452250B2 (en)2009-06-252016-09-27Sorin Group Deutschland GmbhDevice for pumping blood in an extracorporeal circuit
US9492326B2 (en)2004-04-052016-11-15Bluesky Medical Group IncorporatedReduced pressure wound treatment system
US20160375185A1 (en)*2014-02-242016-12-29Fresenius Kabi Deutschland GmbhApparatus and method for determining the liquid level of salvaged blood in a blood collection reservoir of an autologous blood transfusion system
US9763609B2 (en)2003-07-252017-09-19Dexcom, Inc.Analyte sensors having a signal-to-noise ratio substantially unaffected by non-constant noise
US9986942B2 (en)2004-07-132018-06-05Dexcom, Inc.Analyte sensor
US10010658B2 (en)2013-05-102018-07-03Smith & Nephew PlcFluidic connector for irrigation and aspiration of wounds
US10046096B2 (en)2012-03-122018-08-14Smith & Nephew PlcReduced pressure apparatus and methods
US10058642B2 (en)2004-04-052018-08-28Bluesky Medical Group IncorporatedReduced pressure treatment system
WO2018206941A1 (en)*2017-05-122018-11-15University Of StrathclydeLimb stabilisation apparatus and methods
US10159980B2 (en)2013-08-022018-12-25All Cell Recovery LLCSystems and methods for recovering blood cells, in a controlled environment, for storage
US10213541B2 (en)2011-07-122019-02-26Sorin Group Italia S.R.L.Dual chamber blood reservoir
US10300183B2 (en)*2012-05-302019-05-28Lifecell CorporationDevice for harvesting, processing and transferring adipose tissue
US10335531B2 (en)2013-09-242019-07-02Keith GipsonSystem and method for cardiopulmonary bypass using hypobaric oxygenation
US10384041B2 (en)2005-09-072019-08-20Smith & Nephew, Inc.Self contained wound dressing apparatus
US10413644B2 (en)2004-04-272019-09-17Smith & Nephew PlcWound treatment apparatus and method
US10458833B2 (en)2014-05-162019-10-29Sorin Group Italia S.R.L.Blood reservoir with fluid volume measurement based on pressure sensor
US10463773B2 (en)2005-09-072019-11-05Smith & Nephew, Inc.Wound dressing with vacuum reservoir
US10610136B2 (en)2005-03-102020-04-07Dexcom, Inc.System and methods for processing analyte sensor data for sensor calibration
US10791928B2 (en)2007-05-182020-10-06Dexcom, Inc.Analyte sensors having a signal-to-noise ratio substantially unaffected by non-constant noise
USD898925S1 (en)2018-09-132020-10-13Smith & Nephew PlcMedical dressing
US10813577B2 (en)2005-06-212020-10-27Dexcom, Inc.Analyte sensor
US10835672B2 (en)2004-02-262020-11-17Dexcom, Inc.Integrated insulin delivery system with continuous glucose sensor
US10898388B2 (en)2015-04-272021-01-26Smith & Nephew PlcReduced pressure apparatuses and methods
US10912869B2 (en)2008-05-212021-02-09Smith & Nephew, Inc.Wound therapy system with related methods therefor
US10966609B2 (en)2004-02-262021-04-06Dexcom, Inc.Integrated medicament delivery device for use with continuous analyte sensor
US10980461B2 (en)2008-11-072021-04-20Dexcom, Inc.Advanced analyte sensor calibration and error detection
US11000215B1 (en)2003-12-052021-05-11Dexcom, Inc.Analyte sensor
US11058807B2 (en)2008-03-122021-07-13Smith & Nephew, Inc.Negative pressure dressing and method of using same
US11096831B2 (en)2016-05-032021-08-24Smith & Nephew PlcNegative pressure wound therapy device activation and control
US20210268163A1 (en)*2018-11-272021-09-02Terumo Kabushiki KaishaOxygenator
US11116669B2 (en)2016-08-252021-09-14Smith & Nephew PlcAbsorbent negative pressure wound therapy dressing
US11123471B2 (en)2017-03-082021-09-21Smith & Nephew PlcNegative pressure wound therapy device control in presence of fault condition
US11135343B2 (en)*2016-12-012021-10-05Fenwal, Inc.Blood component pooling device, system and method
US11148109B2 (en)*2016-11-162021-10-19Zyno Medical, LlcIsolatable automatic drug compounding system
US11160915B2 (en)2017-05-092021-11-02Smith & Nephew PlcRedundant controls for negative pressure wound therapy systems
US11173240B2 (en)2016-05-032021-11-16Smith & Nephew PlcOptimizing power transfer to negative pressure sources in negative pressure therapy systems
US11246990B2 (en)2004-02-262022-02-15Dexcom, Inc.Integrated delivery device for continuous glucose sensor
US11266825B2 (en)*2020-02-202022-03-08First Pass, LlcManual clot aspiration and filtration system and method of removing a clot
US20220080094A1 (en)*2019-06-272022-03-17Livanova Deutschland GmbhDevice for Automatically Establishing the Venous Inflow to a Blood Reservoir of an Extracorporeal Blood Circulation System
US11285047B2 (en)2016-04-262022-03-29Smith & Nephew PlcWound dressings and methods of use with integrated negative pressure source having a fluid ingress inhibition component
US11298453B2 (en)2003-10-282022-04-12Smith & Nephew PlcApparatus and method for wound cleansing with actives
US11305047B2 (en)2016-05-032022-04-19Smith & Nephew PlcSystems and methods for driving negative pressure sources in negative pressure therapy systems
CN114470384A (en)*2022-02-172022-05-13四川大学华西医院Negative pressure type extracorporeal circulation blood suction system
US11331022B2 (en)2017-10-242022-05-17Dexcom, Inc.Pre-connected analyte sensors
US11350862B2 (en)2017-10-242022-06-07Dexcom, Inc.Pre-connected analyte sensors
US11365728B2 (en)2017-02-242022-06-21Quanta Dialysis Technologies Ltd.Testing rotor engagement of a rotary peristaltic pump
US11399745B2 (en)2006-10-042022-08-02Dexcom, Inc.Dual electrode system for a continuous analyte sensor
US11439333B2 (en)*2019-01-182022-09-13Becton, Dickinson And CompanyBlood collection system including a baffle
US11497653B2 (en)2017-11-012022-11-15Smith & Nephew PlcNegative pressure wound treatment apparatuses and methods with integrated electronics
CN115475288A (en)*2021-05-312022-12-16深圳麦科田生命科学有限公司Suction device and suction method
US11541161B2 (en)2016-06-242023-01-03Haemonetics CorporationSystem and method for continuous flow red blood cell washing
US11554203B2 (en)2017-11-012023-01-17Smith & Nephew PlcNegative pressure wound treatment apparatuses and methods with integrated electronics
US11564847B2 (en)2016-09-302023-01-31Smith & Nephew PlcNegative pressure wound treatment apparatuses and methods with integrated electronics
US11564845B2 (en)2017-09-132023-01-31Smith & Nephew PlcNegative pressure wound treatment apparatuses and methods with integrated electronics
US11571499B2 (en)2015-12-302023-02-07Quanta Dialysis Technologies Ltd.Dialysis machine
US11583618B2 (en)2014-06-022023-02-21Quanta Dialysis Technologies LimitedMethod of heat sanitization of a haemodialysis water circuit using a calculated dose
US11633133B2 (en)2003-12-052023-04-25Dexcom, Inc.Dual electrode system for a continuous analyte sensor
US11660382B2 (en)2016-12-232023-05-30Quanta Dialysis Technologies LimitedValve leak detection system
US11701265B2 (en)2017-09-132023-07-18Smith & Nephew PlcNegative pressure wound treatment apparatuses and methods with integrated electronics
US11707564B2 (en)2017-11-012023-07-25Smith & Nephew PlcSafe operation of integrated negative pressure wound treatment apparatuses
US11717602B2 (en)2016-08-302023-08-08Lifecell CorporationSystems and methods for medical device control
US11723809B2 (en)2016-03-072023-08-15Smith & Nephew PlcWound treatment apparatuses and methods with negative pressure source integrated into wound dressing
US20240033408A1 (en)*2022-07-282024-02-01Cardiacassist, Inc.Extracorporeal life support system with blood recirculation pathway
USRE49881E1 (en)2013-03-282024-03-26Quanta Fluid Solutions Ltd.Re-use of a hemodialysis cartridge
US20240173042A1 (en)*2021-10-182024-05-30Imperative Care, Inc.Device for clot retrieval with varying tube diameters
USRE50004E1 (en)2013-08-142024-06-11Quanta Dialysis Technologies Ltd.Dual haemodialysis and haemodiafiltration blood treatment device
US12005182B2 (en)2019-05-312024-06-11T.J.Smith And Nephew, LimitedSystems and methods for extending operational time of negative pressure wound treatment apparatuses
US12005181B2 (en)2016-12-122024-06-11Smith & Nephew PlcPressure wound therapy status indication via external device
US12011528B2 (en)2017-02-022024-06-18Quanta Dialysis Technologies Ltd.Phased convective operation
US12083263B2 (en)2019-03-202024-09-10Smith & Nephew PlcNegative pressure wound treatment apparatuses and methods with integrated electronics
CN119098054A (en)*2024-09-052024-12-10洁翼流体技术(上海)有限公司 A ceramic membrane microfiltration device for separating milk whey protein
US12163513B2 (en)2016-02-102024-12-10Quanta Dialysis Technologies Ltd.Membrane pump usage condition detection
US12178467B2 (en)2011-03-152024-12-31Angiodynamics, Inc.Device and method for removing material from a hollow anatomical structure
US12245781B2 (en)2007-12-202025-03-11Angiodynamics, Inc.Systems and methods for removing undesirable material within a circulatory system
US12245788B2 (en)2011-03-152025-03-11Angiodynamics, Inc.Device and method for removing material from a hollow anatomical structure
US12251504B2 (en)*2017-06-302025-03-18Quanta Dialysis Technologies Ltd.Dialysis systems, devices and methods
USD1070090S1 (en)2017-09-282025-04-08Quanta Dialysis Technologies Ltd.Dialysis machine
US12311093B2 (en)2020-02-202025-05-27First Pass, LlcManual clot aspiration and filtration system and method of removing a clot
US12318097B2 (en)2007-12-202025-06-03Angiodynamics, Inc.Systems and methods for removing undesirable material within a circulatory system
US12357738B2 (en)2019-05-312025-07-15Quanta Dialysis Technologies LimitedSource container connector

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US5755683A (en)*1995-06-071998-05-26Deka Products Limited PartnershipStopcock valve
DE10162931B4 (en)*2001-12-202005-11-03Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Apparatus and method for separating inhomogeneous biological tissue
WO2010036338A1 (en)2008-09-242010-04-01Jerry ShevitzScreen filter module for alternating flow filtration
CN103298538B (en)*2010-08-252017-05-10瑞普利根公司 Fluid Filtration System
KR101890000B1 (en)*2011-02-102018-08-20얀센 백신스 앤드 프리벤션 비.브이.Pneumatic alternating pressure membrane cell separation system
JP5951252B2 (en)*2011-12-282016-07-13日機装株式会社 Separation liquid return device
JP7039477B2 (en)2015-11-102022-03-22レプリゲン・コーポレイション Disposable filtration unit with alternating tangential flow
EP4121138A2 (en)2020-03-202023-01-25Hemoclear BVBlood separation system and blood products

Citations (18)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US2804075A (en)*1955-11-141957-08-27Ruth O BordenNon-clogging surgical aspirator
US3896733A (en)*1973-10-181975-07-29Pall CorpAutotransfusion apparatus
US3965896A (en)*1974-06-171976-06-29Swank Roy LBlood autotransfusion method and apparatus
US3993067A (en)*1975-04-241976-11-23Sherwood Medical Industries Inc.Autotransfusion device
US4006745A (en)*1975-05-221977-02-08Sorenson Research Co., Inc.Autologous transfusion system and method
US4014329A (en)*1975-07-031977-03-29The Rochester General HospitalMethod and apparatus for autotransfusion of blood
US4033345A (en)*1975-11-131977-07-05Sorenson Research Co., Inc.Autologous transfusion filter system and method
US4047526A (en)*1975-05-221977-09-13Sorenson Research Co., Inc.Autologous blood system and method
US4631050A (en)*1985-09-241986-12-23Reed Charles CAutotransfusion system and method
US4744785A (en)*1984-10-021988-05-17C. R. Bard, Inc.Autotransfusion system
US4772256A (en)*1986-11-071988-09-20Lantech, Inc.Methods and apparatus for autotransfusion of blood
US4796644A (en)*1985-07-111989-01-10Fresenius AgApparatus for infusion and removal of samples of blood and other body fluids
US4798578A (en)*1987-02-131989-01-17Sherwood Medical CompanyAutotransfusion device
US4867738A (en)*1987-09-141989-09-19International Technidyne CorporationApparatus and methods for utilizing autotransfusion systems and related equipment
US4874359A (en)*1987-12-141989-10-17White Frederick RPower infuser
US4886487A (en)*1985-11-181989-12-12Gambro AbAutotransfusion apparatus
US4898572A (en)*1986-06-241990-02-06Futur-Quotidien S.A.Autotransfuser
US4976682A (en)*1987-11-231990-12-11Lane Perry LMethods and apparatus for autologous blood recovery

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
DE3762480D1 (en)*1986-08-231990-06-07Arno W Latzke AGENT FOR APPLICATION OF TRANSDERMAL RESORBABLE ACTIVE SUBSTANCES.

Patent Citations (18)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US2804075A (en)*1955-11-141957-08-27Ruth O BordenNon-clogging surgical aspirator
US3896733A (en)*1973-10-181975-07-29Pall CorpAutotransfusion apparatus
US3965896A (en)*1974-06-171976-06-29Swank Roy LBlood autotransfusion method and apparatus
US3993067A (en)*1975-04-241976-11-23Sherwood Medical Industries Inc.Autotransfusion device
US4006745A (en)*1975-05-221977-02-08Sorenson Research Co., Inc.Autologous transfusion system and method
US4047526A (en)*1975-05-221977-09-13Sorenson Research Co., Inc.Autologous blood system and method
US4014329A (en)*1975-07-031977-03-29The Rochester General HospitalMethod and apparatus for autotransfusion of blood
US4033345A (en)*1975-11-131977-07-05Sorenson Research Co., Inc.Autologous transfusion filter system and method
US4744785A (en)*1984-10-021988-05-17C. R. Bard, Inc.Autotransfusion system
US4796644A (en)*1985-07-111989-01-10Fresenius AgApparatus for infusion and removal of samples of blood and other body fluids
US4631050A (en)*1985-09-241986-12-23Reed Charles CAutotransfusion system and method
US4886487A (en)*1985-11-181989-12-12Gambro AbAutotransfusion apparatus
US4898572A (en)*1986-06-241990-02-06Futur-Quotidien S.A.Autotransfuser
US4772256A (en)*1986-11-071988-09-20Lantech, Inc.Methods and apparatus for autotransfusion of blood
US4798578A (en)*1987-02-131989-01-17Sherwood Medical CompanyAutotransfusion device
US4867738A (en)*1987-09-141989-09-19International Technidyne CorporationApparatus and methods for utilizing autotransfusion systems and related equipment
US4976682A (en)*1987-11-231990-12-11Lane Perry LMethods and apparatus for autologous blood recovery
US4874359A (en)*1987-12-141989-10-17White Frederick RPower infuser

Cited By (540)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US5407425A (en)*1989-12-291995-04-18Werner; MargritSystem for the collecting and retransfusion of autologous blood
US5234403A (en)*1990-05-251993-08-10Sumitomo Bakelite Co., Ltd.Blood collecting apparatus
US6990982B1 (en)1990-06-282006-01-31Bonutti Ip, LlcMethod for harvesting and processing cells from tissue fragments
US7896880B2 (en)1990-06-282011-03-01P Tech, LlcApparatus and method for tissue removal
US20020099401A1 (en)*1990-06-282002-07-25Bonutti Petel M.Apparatus and method for tissue removal
US7134437B2 (en)*1990-06-282006-11-14Bonutti Ip, LlcMethod for utilizing human tissue
WO1993001858A1 (en)*1991-07-161993-02-04Asahi Medical Co., LtdAutotransfusion membrane system
US7462200B2 (en)1991-08-122008-12-09Marctec, LlcMethod for tissue grafting
US20030130744A1 (en)*1991-08-122003-07-10Bonutti Peter M.Tissue cage
US7727283B2 (en)1991-08-122010-06-01P Tech, Llc.Tissue stabilizing implant method
JP3186770B2 (en)1991-11-152001-07-11デカ・プロダクツ・リミテッド・パートナーシップ Intravenous injection device having air removal means
US5484469A (en)*1992-02-141996-01-16Hoeganaes CorporationMethod of making a sintered metal component and metal powder compositions therefor
US5330425A (en)*1992-04-301994-07-19Utterberg David SBlow molded venous drip chamber for hemodialysis
US5665061A (en)*1992-08-111997-09-09Cobe Laboratories, Inc.Biological/pharmaceutical method and apparatus for collecting and mixing fluids
US5378227A (en)*1992-08-111995-01-03Cobe Laboratories, Inc.Biological/pharmaceutical method and apparatus for collecting and mixing fluids
EP0636379A1 (en)*1993-06-281995-02-01C.R. Bard, Inc.Disposable blood washing and apheresis device
US5554293A (en)*1993-06-281996-09-10C. R. Bard, Inc.Disposable blood washing and apheresis device and method of using thereof
US20040154974A1 (en)*1993-12-222004-08-12Baxter International Inc.Method of making a filter assembly having a flexible housing
US6422397B1 (en)1993-12-222002-07-23Baxter International, Inc.Blood collection systems including an integral, flexible filter
US6367634B1 (en)1993-12-222002-04-09Baxter International Inc.Blood collection systems including an integral, flexible filter
US7278541B2 (en)1993-12-222007-10-09Fenwal, Inc.Method of making a filter assembly having a flexible housing
US6745902B2 (en)1993-12-222004-06-08Baxter International Inc.Blood collection systems including an integral, flexible filter
US20040149646A1 (en)*1993-12-222004-08-05Baxter International Inc.Blood collection systems including a flexible filter
US6688476B2 (en)1993-12-222004-02-10Baxter International Inc.Filter assembly having a flexible housing and method of making same
US7353956B2 (en)1993-12-222008-04-08Fenwal, Inc.Blood collection systems including a flexible filter
US5441482A (en)*1994-05-111995-08-15The Regents Of The University Of MinnesotaJet driven surgical suction device and method of using
US7332125B2 (en)1994-10-132008-02-19Haemonetics CorporationSystem and method for processing blood
US20040147865A1 (en)*1994-10-132004-07-29Cianci James P.System and method for processing blood
US5674394A (en)*1995-03-241997-10-07Johnson & Johnson Medical, Inc.Single use system for preparation of autologous plasma
US6197194B1 (en)1995-03-242001-03-06Elaine WhitmoreSingle use system for preparing autologous plasma and fibrin gel
US6001259A (en)*1995-03-241999-12-14Johnson & Johnson Medical, Inc.Preparation of autologous plasma and fibrin gel
US5656027A (en)*1995-06-061997-08-12Cobe Laboratories, Inc.Surgical fluid suction accumulator and volume measurement device
US5743894A (en)*1995-06-071998-04-28Sherwood Medical CompanySpike port with integrated two way valve access
US5971948A (en)*1995-12-131999-10-26Haemonetics CorporationApparatus for collection, washing, and reinfusion of shed blood
US5795159A (en)*1996-02-021998-08-18The United States Of America As Represented By The Secretary Of The NavyMercury removal method and apparatus
US5931821A (en)*1996-03-051999-08-03Tyco Group S.A.R.L.Chest drainage unit with controlled automatic excess negativity relief feature
US5770073A (en)*1996-03-151998-06-23Minntech CorporationCombined cardiotomy and venous reservoir
US5925025A (en)*1996-06-051999-07-20Tyco Group S.A.R.L.Filtration valve cap with reflux clearing feature and related method of use thereof
US6808675B1 (en)1996-06-252004-10-26Thermogenesis Corp.Freezing and thawing bag, mold, apparatus and method
US6232115B1 (en)1996-06-252001-05-15Thermogenesis Corp.Freezing and thawing bag, mold, apparatus and method
US6213334B1 (en)1996-09-052001-04-10Baxter International IncFlexible, three-dimensional containers and methods for making them
WO1998029149A1 (en)*1997-01-031998-07-09Shettigar U RamakrishnaIntraoperative blood salvaging system and method
US6099493A (en)*1997-05-062000-08-08Sherwood Services, AgContinuous autotransfusion filtration system
US5993406A (en)*1997-05-141999-11-30Cedars-Sinai Medical CenterArtificial gut
US6379619B1 (en)1997-05-142002-04-30Cedars-Sinai Medical CenterArtificial gut
US6217544B1 (en)1997-05-302001-04-17Sherwood Services, AgFiltration valve cap with reflux clearing feature and related method of use thereof
US5876611A (en)*1997-06-161999-03-02Shettigar; U. RamakrishnaIntraoperative blood salvaging system and method
US6017493A (en)*1997-09-262000-01-25Baxter International Inc.Vacuum-assisted venous drainage reservoir for CPB systems
US6537495B1 (en)1997-09-262003-03-25Edwards Lifesciences LlcVacuum-assisted venous drainage system with rigid housing and flexible reservoir
US6361642B1 (en)1997-12-022002-03-26Baxter International Inc.Heat and pressure-formed flexible containers
US5989438A (en)*1997-12-121999-11-23Baxter International Inc.Active blood filter and method for active blood filtration
US6251295B1 (en)*1998-01-082001-06-26Nexell Therapeutics Inc.Method for recirculation washing of blood cells
US20010035377A1 (en)*1998-01-082001-11-01Nexell Therapeutics Inc.Recirculation container
US6555360B1 (en)*1998-03-302003-04-29Friedrich SriencFlow injection flow cytometry system for on-line monitoring of biroreactors and method for monitoring
EP1121175A4 (en)*1998-10-162005-09-21Mission Medical IncBlood processing system
US6695803B1 (en)1998-10-162004-02-24Mission Medical, Inc.Blood processing system
US7008393B2 (en)1998-10-162006-03-07Mission Medical, Inc.Blood processing system
US6817984B2 (en)1998-10-162004-11-16Mission Medical, Inc.Blood processing system
US6547775B1 (en)1998-10-222003-04-15Medtronic, Inc.Atraumatic blood suction system
US6251291B1 (en)1998-12-282001-06-26Tranfusion Technologies CorporationReservoir-and-filter system and method of use
US6524267B1 (en)*1999-02-172003-02-25Medtronic, Inc.Venous filter for assisted venous return
US6918887B1 (en)1999-02-172005-07-19Medtronic, Inc.Venous filter for assisted venous return
US6302860B1 (en)*1999-02-172001-10-16Medtronic, Inc.Venous filter for assisted venous return
US6601710B2 (en)1999-04-202003-08-05Baxter International Inc.Filter assembly having a flexible housing
US20030209479A1 (en)*2000-07-102003-11-13Lynn Daniel RBlood filters, blood collection and processing systems, and methods therefore
US20020031836A1 (en)*2000-09-112002-03-14Feldstein Mark J.Fluidics system
US20020096467A1 (en)*2000-12-012002-07-25Jean-Marc CappiaChemical process system with multi-functional barrier filter
US6902671B2 (en)*2000-12-012005-06-07Millipore CorporationChemical process system with multi-functional barrier filter
US6960322B2 (en)2001-02-092005-11-01Cardiovention, Inc.Integrated blood handling system having active gas removal system and methods of use
US20040009097A1 (en)*2001-02-092004-01-15Cardiovention, Inc.Integrated blood handling system having active gas removal system and methods of use
US20060029515A1 (en)*2001-02-092006-02-09Cardiovention, Inc.Integrated blood handling system having active gas removal system and method of use
US20040228760A1 (en)*2001-02-092004-11-18Cardiovention, Inc.Methods of use of a blood filter having a sensor for active gas removal
US6773670B2 (en)2001-02-092004-08-10Cardiovention, Inc. C/O The Brenner Group, Inc.Blood filter having a sensor for active gas removal and methods of use
US6730267B2 (en)2001-02-092004-05-04Cardiovention, Inc.Integrated blood handling system having active gas removal system and methods of use
US7541000B2 (en)2001-02-092009-06-02Cardiovention, Inc.Micro-processor controlled active gas removal apparatus
US6632192B2 (en)*2001-03-052003-10-14Transvivo, Inc.Apparatus and method for selective reduction of segmental intracellular and extracellular edema
US7013703B2 (en)2001-03-202006-03-21Therox, Inc.System and method of evaluating or calibrating a bubble detector
US6843099B2 (en)*2001-03-202005-01-18Therox, Inc.Bubble detector and method of evaluation or calibration thereof
US20040089050A1 (en)*2001-03-202004-05-13Daw Derek J.Bubble detector and method of evaluation or calibration thereof
US20040154374A1 (en)*2001-03-202004-08-12Daw Derek J.System and method of evaluating or calibrating a bubble detector
US20040214314A1 (en)*2001-11-022004-10-28Friedrich SriencHigh throughput bioreactor
US20090081770A1 (en)*2001-11-022009-03-26Regents Of The University Of MinnesotaHigh throughput bioreactor
US7901937B2 (en)2001-11-022011-03-08Regents Of The University Of MinnesotaHigh throughput bioreactor
US20030233064A1 (en)*2002-04-242003-12-18Interpore OrthopaedicsBlood separation and concentration system
US7806845B2 (en)2002-04-242010-10-05Biomet Biologics, LlcBlood separation and concentration system
US8361005B2 (en)2002-04-242013-01-29Biomet Biologics, LlcBlood separation and concentration system
US20110003276A1 (en)*2002-04-242011-01-06Biomet Biologics, LlcBlood separation and concentration system
WO2003090839A1 (en)*2002-04-242003-11-06Interpore OrthopaedicsBlood separation and concentration system
US9526821B2 (en)2002-04-242016-12-27Biomet Biologics, LlcBlood separation and concentration system
US8961445B2 (en)2002-04-242015-02-24Biomet Biologics, LlcBlood separation and concentration system
US8543184B2 (en)2002-05-222013-09-24Dexcom, Inc.Silicone based membranes for use in implantable glucose sensors
US8064977B2 (en)2002-05-222011-11-22Dexcom, Inc.Silicone based membranes for use in implantable glucose sensors
US11020026B2 (en)2002-05-222021-06-01Dexcom, Inc.Silicone based membranes for use in implantable glucose sensors
US7613491B2 (en)2002-05-222009-11-03Dexcom, Inc.Silicone based membranes for use in implantable glucose sensors
US9549693B2 (en)2002-05-222017-01-24Dexcom, Inc.Silicone based membranes for use in implantable glucose sensors
US10052051B2 (en)2002-05-222018-08-21Dexcom, Inc.Silicone based membranes for use in implantable glucose sensors
EP1374929A1 (en)*2002-06-252004-01-02Jostra AGApparatus for elimination of gas bubbles
US20040019310A1 (en)*2002-07-292004-01-29Michael HogendijkBlood aspiration system and methods of use
US7223253B2 (en)2002-07-292007-05-29Gore Enterprise Holdings, Inc.Blood aspiration system and methods of use
US8545464B2 (en)2002-09-032013-10-01Bluesky Medical Group IncorporatedReduced pressure treatment system
US8628505B2 (en)2002-09-032014-01-14Bluesky Medical Group IncorporatedReduced pressure treatment system
US8118794B2 (en)2002-09-032012-02-21Bluesky Medical Group, Inc.Reduced pressure treatment system
US10265445B2 (en)2002-09-032019-04-23Smith & Nephew, Inc.Reduced pressure treatment system
US9211365B2 (en)2002-09-032015-12-15Bluesky Medical Group, Inc.Reduced pressure treatment system
US11376356B2 (en)2002-09-032022-07-05Smith & Nephew, Inc.Reduced pressure treatment system
US11298454B2 (en)2002-09-032022-04-12Smith & Nephew, Inc.Reduced pressure treatment system
US9205001B2 (en)2002-10-282015-12-08Smith & Nephew PlcApparatus for aspirating, irrigating and cleansing wounds
US10842678B2 (en)2002-10-282020-11-24Smith & Nephew PlcApparatus for aspirating, irrigating and cleansing wounds
US9844473B2 (en)2002-10-282017-12-19Smith & Nephew PlcApparatus for aspirating, irrigating and cleansing wounds
US8398614B2 (en)2002-10-282013-03-19Smith & Nephew PlcApparatus for aspirating, irrigating and cleansing wounds
US9844474B2 (en)2002-10-282017-12-19Smith & Nephew PlcApparatus for aspirating, irrigating and cleansing wounds
US8834451B2 (en)2002-10-282014-09-16Smith & Nephew PlcIn-situ wound cleansing apparatus
US8535296B2 (en)2002-10-282013-09-17Smith & Nephew PlcApparatus for aspirating, irrigating and cleansing wounds
US9387126B2 (en)2002-10-282016-07-12Smith & Nephew PlcApparatus for aspirating, irrigating and cleansing wounds
US10278869B2 (en)2002-10-282019-05-07Smith & Nephew PlcApparatus for aspirating, irrigating and cleansing wounds
US7335334B2 (en)2003-01-142008-02-26Medtronic, Inc.Active air removal from an extracorporeal blood circuit
US7198751B2 (en)2003-01-142007-04-03Medtronic, Inc.Disposable, integrated, extracorporeal blood circuit
US20040195178A1 (en)*2003-01-142004-10-07Carpenter Walter L.Extracorporeal blood circuit priming system and method
US7829018B2 (en)2003-01-142010-11-09Medtronic, Inc.Active air removal from an extracorporeal blood circuit
US7189352B2 (en)2003-01-142007-03-13Medtronic, Inc.Extracorporeal blood circuit priming system and method
US7704455B2 (en)2003-01-142010-04-27Medtronic, Inc.Active air removal system operating modes of an extracorporeal blood circuit
US20040220509A1 (en)*2003-01-142004-11-04Olsen Robert W.Active air removal from an extracorporeal blood circuit
US7201870B2 (en)2003-01-142007-04-10Medtronic, Inc.Active air removal system operating modes of an extracorporeal blood circuit
US7740800B2 (en)2003-01-142010-06-22Medtronic, Inc.Extracorporeal blood circuit air removal system and method
US7204958B2 (en)2003-01-142007-04-17Medtronic, Inc.Extracorporeal blood circuit air removal system and method
US20050063860A1 (en)*2003-01-142005-03-24Carpenter Walter L.Disposable, integrated, extracorporeal blood circuit
US20040197223A1 (en)*2003-01-142004-10-07Olsen Robert W.Active air removal system operating modes of an extracorporeal blood circuit
US20070140899A1 (en)*2003-01-142007-06-21Olsen Robert WActive air removal system operating modes of an extracorporeal blood circuit
US20040184953A1 (en)*2003-03-172004-09-23Litzie A. KennethExtracorporeal blood handling system with automatic flow control and methods of use
US7022099B2 (en)2003-03-172006-04-04Cardiovention, Inc.Extracorporeal blood handling system with automatic flow control and methods of use
US20040238444A1 (en)*2003-05-272004-12-02Michael RagusaContinuous blood filtration and method of use
US7601268B2 (en)2003-05-272009-10-13Haemonetics CorporationContinuous blood filtration and method of use
US8364229B2 (en)2003-07-252013-01-29Dexcom, Inc.Analyte sensors having a signal-to-noise ratio substantially unaffected by non-constant noise
US9763609B2 (en)2003-07-252017-09-19Dexcom, Inc.Analyte sensors having a signal-to-noise ratio substantially unaffected by non-constant noise
US10376143B2 (en)2003-07-252019-08-13Dexcom, Inc.Analyte sensors having a signal-to-noise ratio substantially unaffected by non-constant noise
US10052055B2 (en)2003-08-012018-08-21Dexcom, Inc.Analyte sensor
US8886273B2 (en)2003-08-012014-11-11Dexcom, Inc.Analyte sensor
US8626257B2 (en)2003-08-012014-01-07Dexcom, Inc.Analyte sensor
US9289542B2 (en)2003-10-282016-03-22Smith & Nephew PlcWound cleansing apparatus
US20070129707A1 (en)*2003-10-282007-06-07Blott Patrick LWound cleansing apparatus with heat
US11857746B2 (en)2003-10-282024-01-02Smith & Nephew PlcWound cleansing apparatus in-situ
US9446178B2 (en)2003-10-282016-09-20Smith & Nephew PlcWound cleansing apparatus in-situ
US20100274167A1 (en)*2003-10-282010-10-28Smith & Nephew PlcWound cleansing apparatus with scaffold
US11298453B2 (en)2003-10-282022-04-12Smith & Nephew PlcApparatus and method for wound cleansing with actives
US8758313B2 (en)2003-10-282014-06-24Smith & Nephew PlcApparatus and method for wound cleansing with actives
US7964766B2 (en)2003-10-282011-06-21Smith & Nephew PlcWound cleansing apparatus in-situ
US8569566B2 (en)*2003-10-282013-10-29Smith & Nephew, PlcWound cleansing apparatus in-situ
US8080702B2 (en)2003-10-282011-12-20Smith & Nephew PlcWound cleansing apparatus in-situ
US7794450B2 (en)*2003-10-282010-09-14Smith & Nephew PlcWound cleansing apparatus with heat
US8128615B2 (en)2003-10-282012-03-06Smith & Nephew PlcWound cleansing apparatus with scaffold
US9616208B2 (en)2003-10-282017-04-11Smith & Nephew PlcWound cleansing apparatus
US9452248B2 (en)2003-10-282016-09-27Smith & Nephew PlcWound cleansing apparatus in-situ
US8926592B2 (en)2003-10-282015-01-06Smith & Nephew PlcWound cleansing apparatus with heat
US20070066945A1 (en)*2003-10-282007-03-22Martin Robin PWound cleansing apparatus with scaffold
US20120109084A1 (en)*2003-10-282012-05-03Smith & Nephew PlcWound cleansing apparatus in-situ
US7699830B2 (en)2003-10-282010-04-20Smith & Nephew PlcWound cleansing apparatus with scaffold
US8882746B2 (en)2003-10-282014-11-11Smith & Nephew PlcWound cleansing apparatus with scaffold
US20070167926A1 (en)*2003-10-282007-07-19Blott Patrick LWound cleansing apparatus in-situ
US8257327B2 (en)2003-10-282012-09-04Smith & Nephew PlcWound cleansing apparatus with actives
US20050101261A1 (en)*2003-11-102005-05-12Ronald LachmanBluetooth interface between cellular and wired telephone networks
US11633133B2 (en)2003-12-052023-04-25Dexcom, Inc.Dual electrode system for a continuous analyte sensor
US11020031B1 (en)2003-12-052021-06-01Dexcom, Inc.Analyte sensor
US8287453B2 (en)2003-12-052012-10-16Dexcom, Inc.Analyte sensor
US8425417B2 (en)2003-12-052013-04-23Dexcom, Inc.Integrated device for continuous in vivo analyte detection and simultaneous control of an infusion device
US11000215B1 (en)2003-12-052021-05-11Dexcom, Inc.Analyte sensor
US7762976B2 (en)2004-01-202010-07-27Sorin Group Deutschland GmbhAutomatic air removal system
US12226617B2 (en)2004-02-262025-02-18Dexcom, Inc.Integrated delivery device for continuous glucose sensor
US10966609B2 (en)2004-02-262021-04-06Dexcom, Inc.Integrated medicament delivery device for use with continuous analyte sensor
US12115357B2 (en)2004-02-262024-10-15Dexcom, Inc.Integrated delivery device for continuous glucose sensor
US12102410B2 (en)2004-02-262024-10-01Dexcom, IncIntegrated medicament delivery device for use with continuous analyte sensor
US11246990B2 (en)2004-02-262022-02-15Dexcom, Inc.Integrated delivery device for continuous glucose sensor
US10835672B2 (en)2004-02-262020-11-17Dexcom, Inc.Integrated insulin delivery system with continuous glucose sensor
US10058642B2 (en)2004-04-052018-08-28Bluesky Medical Group IncorporatedReduced pressure treatment system
US10350339B2 (en)2004-04-052019-07-16Smith & Nephew, Inc.Flexible reduced pressure treatment appliance
US11730874B2 (en)2004-04-052023-08-22Smith & Nephew, Inc.Reduced pressure treatment appliance
US10105471B2 (en)2004-04-052018-10-23Smith & Nephew, Inc.Reduced pressure treatment system
US10842919B2 (en)2004-04-052020-11-24Smith & Nephew, Inc.Reduced pressure treatment system
US8282611B2 (en)2004-04-052012-10-09Bluesky Medical Group, Inc.Reduced pressure wound treatment system
US9492326B2 (en)2004-04-052016-11-15Bluesky Medical Group IncorporatedReduced pressure wound treatment system
US9198801B2 (en)2004-04-052015-12-01Bluesky Medical Group, Inc.Flexible reduced pressure treatment appliance
US10363346B2 (en)2004-04-052019-07-30Smith & Nephew, Inc.Flexible reduced pressure treatment appliance
US8449509B2 (en)2004-04-052013-05-28Bluesky Medical Group IncorporatedFlexible reduced pressure treatment appliance
US8303552B2 (en)2004-04-052012-11-06Bluesky Medical Group, Inc.Reduced pressure wound treatment system
US11426497B2 (en)2004-04-272022-08-30Smith & Nephew PlcWound treatment apparatus and method
US8845619B2 (en)2004-04-272014-09-30Smith & Nephew PlcWound treatment apparatus and method
US11617823B2 (en)2004-04-272023-04-04Smith & Nephew PlcWound cleansing apparatus with stress
US11013837B2 (en)2004-04-272021-05-25Smith & Nephew PlcWound treatment apparatus and method
US7753894B2 (en)2004-04-272010-07-13Smith & Nephew PlcWound cleansing apparatus with stress
US20090069759A1 (en)*2004-04-272009-03-12Smith & Nephew , Plc.Apparatus for cleansing wounds with means for supply of thermal energy to the therapy fluid
US10342729B2 (en)2004-04-272019-07-09Smith & Nephew PlcWound cleansing apparatus with stress
US10413644B2 (en)2004-04-272019-09-17Smith & Nephew PlcWound treatment apparatus and method
US20110004171A1 (en)*2004-04-272011-01-06Smith & Nephew PlcWound cleansing apparatus with stress
US8529548B2 (en)2004-04-272013-09-10Smith & Nephew PlcWound treatment apparatus and method
US9526817B2 (en)2004-04-272016-12-27Smith & Nephew PlcWound cleansing apparatus with stress
US9452244B2 (en)2004-04-272016-09-27Smith & Nephew PlcWound cleansing apparatus with stress
US9545463B2 (en)2004-04-282017-01-17Smith & Nephew PlcWound treatment apparatus and method
US10039868B2 (en)2004-04-282018-08-07Smith & Nephew PlcDressing and apparatus for cleansing the wounds
US10758424B2 (en)2004-04-282020-09-01Smith & Nephew PlcDressing and apparatus for cleansing the wounds
US9950100B2 (en)2004-04-282018-04-24Smith & Nephew PlcNegative pressure wound therapy dressing system
US8348910B2 (en)2004-04-282013-01-08Smith & Nephew PlcApparatus for cleansing wounds with means for supply of thermal energy to the therapy fluid
US10758425B2 (en)2004-04-282020-09-01Smith & Nephew PlcNegative pressure wound therapy dressing system
US9044569B2 (en)2004-04-282015-06-02Smith & Nephew PlcWound dressing apparatus and method of use
US9272080B2 (en)2004-05-212016-03-01Bluesky Medical Group IncorporatedFlexible reduced pressure treatment appliance
US8795243B2 (en)2004-05-212014-08-05Bluesky Medical Group IncorporatedFlexible reduced pressure treatment appliance
US9925313B2 (en)2004-05-212018-03-27Smith & Nephew, Inc.Flexible reduced pressure treatment appliance
US10207035B2 (en)2004-05-212019-02-19Smith & Nephew, Inc.Flexible reduced pressure treatment appliance
US11045120B2 (en)2004-07-132021-06-29Dexcom, Inc.Analyte sensor
US7857760B2 (en)2004-07-132010-12-28Dexcom, Inc.Analyte sensor
US10813576B2 (en)2004-07-132020-10-27Dexcom, Inc.Analyte sensor
US10524703B2 (en)2004-07-132020-01-07Dexcom, Inc.Transcutaneous analyte sensor
US8750955B2 (en)2004-07-132014-06-10Dexcom, Inc.Analyte sensor
US7783333B2 (en)2004-07-132010-08-24Dexcom, Inc.Transcutaneous medical device with variable stiffness
US10722152B2 (en)2004-07-132020-07-28Dexcom, Inc.Analyte sensor
US10827956B2 (en)2004-07-132020-11-10Dexcom, Inc.Analyte sensor
US8792953B2 (en)2004-07-132014-07-29Dexcom, Inc.Transcutaneous analyte sensor
US10918313B2 (en)2004-07-132021-02-16Dexcom, Inc.Analyte sensor
US8812072B2 (en)2004-07-132014-08-19Dexcom, Inc.Transcutaneous medical device with variable stiffness
US10799159B2 (en)2004-07-132020-10-13Dexcom, Inc.Analyte sensor
US10932700B2 (en)2004-07-132021-03-02Dexcom, Inc.Analyte sensor
US10918314B2 (en)2004-07-132021-02-16Dexcom, Inc.Analyte sensor
US10918315B2 (en)2004-07-132021-02-16Dexcom, Inc.Analyte sensor
US9986942B2 (en)2004-07-132018-06-05Dexcom, Inc.Analyte sensor
US10980452B2 (en)2004-07-132021-04-20Dexcom, Inc.Analyte sensor
US10993642B2 (en)2004-07-132021-05-04Dexcom, Inc.Analyte sensor
US10709363B2 (en)2004-07-132020-07-14Dexcom, Inc.Analyte sensor
US11883164B2 (en)2004-07-132024-01-30Dexcom, Inc.System and methods for processing analyte sensor data for sensor calibration
US10709362B2 (en)2004-07-132020-07-14Dexcom, Inc.Analyte sensor
US11064917B2 (en)2004-07-132021-07-20Dexcom, Inc.Analyte sensor
US10799158B2 (en)2004-07-132020-10-13Dexcom, Inc.Analyte sensor
US9414777B2 (en)2004-07-132016-08-16Dexcom, Inc.Transcutaneous analyte sensor
US7640048B2 (en)2004-07-132009-12-29Dexcom, Inc.Analyte sensor
US11026605B1 (en)2004-07-132021-06-08Dexcom, Inc.Analyte sensor
US7885697B2 (en)2004-07-132011-02-08Dexcom, Inc.Transcutaneous analyte sensor
US10993641B2 (en)2004-07-132021-05-04Dexcom, Inc.Analyte sensor
US10918316B2 (en)2005-03-102021-02-16Dexcom, Inc.System and methods for processing analyte sensor data for sensor calibration
US10918317B2 (en)2005-03-102021-02-16Dexcom, Inc.System and methods for processing analyte sensor data for sensor calibration
US11000213B2 (en)2005-03-102021-05-11Dexcom, Inc.System and methods for processing analyte sensor data for sensor calibration
US10743801B2 (en)2005-03-102020-08-18Dexcom, Inc.System and methods for processing analyte sensor data for sensor calibration
US10925524B2 (en)2005-03-102021-02-23Dexcom, Inc.System and methods for processing analyte sensor data for sensor calibration
US10716498B2 (en)2005-03-102020-07-21Dexcom, Inc.System and methods for processing analyte sensor data for sensor calibration
US10856787B2 (en)2005-03-102020-12-08Dexcom, Inc.System and methods for processing analyte sensor data for sensor calibration
US11051726B2 (en)2005-03-102021-07-06Dexcom, Inc.System and methods for processing analyte sensor data for sensor calibration
US10617336B2 (en)2005-03-102020-04-14Dexcom, Inc.System and methods for processing analyte sensor data for sensor calibration
US10610135B2 (en)2005-03-102020-04-07Dexcom, Inc.System and methods for processing analyte sensor data for sensor calibration
US10709364B2 (en)2005-03-102020-07-14Dexcom, Inc.System and methods for processing analyte sensor data for sensor calibration
US10610136B2 (en)2005-03-102020-04-07Dexcom, Inc.System and methods for processing analyte sensor data for sensor calibration
US10610137B2 (en)2005-03-102020-04-07Dexcom, Inc.System and methods for processing analyte sensor data for sensor calibration
US10898114B2 (en)2005-03-102021-01-26Dexcom, Inc.System and methods for processing analyte sensor data for sensor calibration
US10918318B2 (en)2005-03-102021-02-16Dexcom, Inc.System and methods for processing analyte sensor data for sensor calibration
CN101146560B (en)*2005-03-242012-03-21Sifr2000股份有限公司Control of bubble formation in extracorporeal circulation
US20090230058A1 (en)*2005-03-242009-09-17Fredrik Boris-MoellerControl of bubble formation in extracorporeal circulation
WO2006101447A1 (en)*2005-03-242006-09-28Sifr 2000 AbControl of bubble formation in extracorporeal circulation
US9044579B2 (en)2005-04-272015-06-02Smith & Nephew PlcWound treatment apparatus and method
US11147714B2 (en)2005-04-272021-10-19Smith & Nephew PlcWound treatment apparatus and method
US10035006B2 (en)2005-04-272018-07-31Smith & Nephew PlcWound treatment apparatus and method
WO2006124307A3 (en)*2005-05-162007-11-01Fox Hollow Technologies IncMethods and systems for filtering aspirated materials
US20060270974A1 (en)*2005-05-162006-11-30Kerberos Proximal Solutions, Inc.Methods and systems for filtering aspirated materials
US10813577B2 (en)2005-06-212020-10-27Dexcom, Inc.Analyte sensor
US11896754B2 (en)2005-09-072024-02-13Smith & Nephew, Inc.Wound dressing with vacuum reservoir
US10384041B2 (en)2005-09-072019-08-20Smith & Nephew, Inc.Self contained wound dressing apparatus
US11737925B2 (en)2005-09-072023-08-29Smith & Nephew, Inc.Self contained wound dressing with micropump
US8829263B2 (en)2005-09-072014-09-09Smith & Nephew, Inc.Self contained wound dressing with micropump
US10201644B2 (en)2005-09-072019-02-12Smith & Nephew, Inc.Self contained wound dressing with micropump
US10463773B2 (en)2005-09-072019-11-05Smith & Nephew, Inc.Wound dressing with vacuum reservoir
US11278658B2 (en)2005-09-072022-03-22Smith & Nephew, Inc.Self contained wound dressing with micropump
US20090204084A1 (en)*2005-09-152009-08-13Patrick Lewis BlottApparatus
US8162909B2 (en)2005-09-152012-04-24Smith & Nephew PlcNegative pressure wound treatment
US8567306B2 (en)*2006-04-032013-10-29Mermaid Co., Ltd.Fryer
US20090101023A1 (en)*2006-04-032009-04-23Mermaid Co., Ltd.Fryer
US8460255B2 (en)2006-05-112013-06-11Kalypto Medical, Inc.Device and method for wound therapy
US10744242B2 (en)2006-05-112020-08-18Smith & Nephew, Inc.Device and method for wound therapy
US11813394B2 (en)2006-05-112023-11-14Smith & Nephew, Inc.Device and method for wound therapy
US12128169B2 (en)2006-05-112024-10-29Smith & Nephew, Inc.Device and method for wound therapy
US11517656B2 (en)2006-05-112022-12-06Smith & Nephew, Inc.Device and method for wound therapy
US20090314724A1 (en)*2006-09-082009-12-24Arno Pieter NierichBlood recuperation device and method
US8187465B2 (en)*2006-09-082012-05-29Gelanus B.V.Blood recuperation device and method
US8366690B2 (en)2006-09-192013-02-05Kci Licensing, Inc.System and method for determining a fill status of a canister of fluid in a reduced pressure treatment system
US8328776B2 (en)2006-09-192012-12-11Kci Licensing, Inc.Reduced pressure treatment system having blockage clearing and dual-zone pressure protection capabilities
US7615007B2 (en)2006-10-042009-11-10Dexcom, Inc.Analyte sensor
US8911367B2 (en)2006-10-042014-12-16Dexcom, Inc.Analyte sensor
US8425416B2 (en)2006-10-042013-04-23Dexcom, Inc.Analyte sensor
US8275438B2 (en)2006-10-042012-09-25Dexcom, Inc.Analyte sensor
US7775975B2 (en)2006-10-042010-08-17Dexcom, Inc.Analyte sensor
US8774886B2 (en)2006-10-042014-07-08Dexcom, Inc.Analyte sensor
US8364230B2 (en)2006-10-042013-01-29Dexcom, Inc.Analyte sensor
US8562528B2 (en)2006-10-042013-10-22Dexcom, Inc.Analyte sensor
US11399745B2 (en)2006-10-042022-08-02Dexcom, Inc.Dual electrode system for a continuous analyte sensor
US8447376B2 (en)2006-10-042013-05-21Dexcom, Inc.Analyte sensor
US9451908B2 (en)2006-10-042016-09-27Dexcom, Inc.Analyte sensor
US8532730B2 (en)2006-10-042013-09-10Dexcom, Inc.Analyte sensor
US8449464B2 (en)2006-10-042013-05-28Dexcom, Inc.Analyte sensor
US8298142B2 (en)2006-10-042012-10-30Dexcom, Inc.Analyte sensor
US8364231B2 (en)2006-10-042013-01-29Dexcom, Inc.Analyte sensor
US11382539B2 (en)2006-10-042022-07-12Dexcom, Inc.Analyte sensor
US8478377B2 (en)2006-10-042013-07-02Dexcom, Inc.Analyte sensor
US10349873B2 (en)2006-10-042019-07-16Dexcom, Inc.Analyte sensor
US20080234641A1 (en)*2007-02-092008-09-25Christopher Brian LockeSystem and method for managing reduced pressure at a tissue site
US8409170B2 (en)*2007-02-092013-04-02Kci Licensing, Inc.System and method for managing reduced pressure at a tissue site
US8827967B2 (en)2007-02-202014-09-09Kci Licensing, Inc.System and method for distinguishing leaks from a disengaged canister condition in a reduced pressure treatment system
US7927319B2 (en)2007-02-202011-04-19Kci Licensing, Inc.System and method for distinguishing leaks from a disengaged canister condition in a reduced pressure treatment system
US10791928B2 (en)2007-05-182020-10-06Dexcom, Inc.Analyte sensors having a signal-to-noise ratio substantially unaffected by non-constant noise
US12433485B2 (en)2007-05-182025-10-07Dexcom, Inc.Analyte sensors having a signal-to-noise ratio substantially unaffected by non-constant noise
US9741139B2 (en)2007-06-082017-08-22Dexcom, Inc.Integrated medicament delivery device for use with continuous analyte sensor
US8562558B2 (en)2007-06-082013-10-22Dexcom, Inc.Integrated medicament delivery device for use with continuous analyte sensor
US10403012B2 (en)2007-06-082019-09-03Dexcom, Inc.Integrated medicament delivery device for use with continuous analyte sensor
US11373347B2 (en)2007-06-082022-06-28Dexcom, Inc.Integrated medicament delivery device for use with continuous analyte sensor
US12394120B2 (en)2007-06-082025-08-19Dexcom, Inc.Integrated medicament delivery device for use with continuous analyte sensor
US9050399B2 (en)2007-07-022015-06-09Smith & Nephew PlcWound treatment apparatus with exudate volume reduction by heat
US9956327B2 (en)2007-07-022018-05-01Smith & Nephew PlcWound treatment apparatus with exudate volume reduction by heat
US8551061B2 (en)2007-07-022013-10-08Smith & Nephew PlcWound treatment apparatus with exudate volume reduction by heat
US20100211031A1 (en)*2007-07-022010-08-19Edward HartwellWound treatment apparatus with exudate volume reduction by heat
US12397113B2 (en)2007-10-092025-08-26Dexcom, Inc.Integrated insulin delivery system with continuous glucose sensor
US12397110B2 (en)2007-10-092025-08-26Dexcom, Inc.Integrated insulin delivery system with continuous glucose sensor
US11744943B2 (en)2007-10-092023-09-05Dexcom, Inc.Integrated insulin delivery system with continuous glucose sensor
US11160926B1 (en)2007-10-092021-11-02Dexcom, Inc.Pre-connected analyte sensors
US12246166B2 (en)2007-10-092025-03-11Dexcom, Inc.Integrated insulin delivery system with continuous glucose sensor
US10182751B2 (en)2007-10-252019-01-22Dexcom, Inc.Systems and methods for processing sensor data
US11272869B2 (en)2007-10-252022-03-15Dexcom, Inc.Systems and methods for processing sensor data
US8417312B2 (en)2007-10-252013-04-09Dexcom, Inc.Systems and methods for processing sensor data
US9717449B2 (en)2007-10-252017-08-01Dexcom, Inc.Systems and methods for processing sensor data
US11045598B2 (en)2007-11-212021-06-29Smith & Nephew PlcVacuum assisted wound dressing
US9956121B2 (en)2007-11-212018-05-01Smith & Nephew PlcWound dressing
US10744041B2 (en)2007-11-212020-08-18Smith & Nephew PlcWound dressing
US11701266B2 (en)2007-11-212023-07-18Smith & Nephew PlcVacuum assisted wound dressing
US9844475B2 (en)2007-11-212017-12-19Smith & Nephew PlcWound dressing
US10231875B2 (en)2007-11-212019-03-19Smith & Nephew PlcWound dressing
US8715256B2 (en)2007-11-212014-05-06Smith & Nephew PlcVacuum assisted wound dressing
US12285318B1 (en)2007-11-212025-04-29Smith & Nephew PlcVacuum assisted wound dressing
US12290627B2 (en)2007-11-212025-05-06Smith & Nephew PlcWound dressing
US8764732B2 (en)2007-11-212014-07-01Smith & Nephew PlcWound dressing
US8808274B2 (en)2007-11-212014-08-19Smith & Nephew PlcWound dressing
US10123909B2 (en)2007-11-212018-11-13Smith & Nephew PlcWound dressing
US11364151B2 (en)2007-11-212022-06-21Smith & Nephew PlcWound dressing
US11351064B2 (en)2007-11-212022-06-07Smith & Nephew PlcWound dressing
US9962474B2 (en)2007-11-212018-05-08Smith & Nephew PlcVacuum assisted wound dressing
US11974902B2 (en)2007-11-212024-05-07Smith & Nephew PlcVacuum assisted wound dressing
US10016309B2 (en)2007-11-212018-07-10Smith & Nephew PlcWound dressing
US10555839B2 (en)2007-11-212020-02-11Smith & Nephew PlcWound dressing
US11110010B2 (en)2007-11-212021-09-07Smith & Nephew PlcWound dressing
US9220822B2 (en)2007-11-212015-12-29Smith & Nephew PlcWound dressing
US11129751B2 (en)2007-11-212021-09-28Smith & Nephew PlcWound dressing
US11179276B2 (en)2007-11-212021-11-23Smith & Nephew PlcWound dressing
US9135402B2 (en)2007-12-172015-09-15Dexcom, Inc.Systems and methods for processing sensor data
US12165757B2 (en)2007-12-172024-12-10Dexcom, Inc.Systems and methods for processing sensor data
US9901307B2 (en)2007-12-172018-02-27Dexcom, Inc.Systems and methods for processing sensor data
US9839395B2 (en)2007-12-172017-12-12Dexcom, Inc.Systems and methods for processing sensor data
US9339238B2 (en)2007-12-172016-05-17Dexcom, Inc.Systems and methods for processing sensor data
US10506982B2 (en)2007-12-172019-12-17Dexcom, Inc.Systems and methods for processing sensor data
US9149233B2 (en)2007-12-172015-10-06Dexcom, Inc.Systems and methods for processing sensor data
US9149234B2 (en)2007-12-172015-10-06Dexcom, Inc.Systems and methods for processing sensor data
US10827980B2 (en)2007-12-172020-11-10Dexcom, Inc.Systems and methods for processing sensor data
US8290559B2 (en)2007-12-172012-10-16Dexcom, Inc.Systems and methods for processing sensor data
US11342058B2 (en)2007-12-172022-05-24Dexcom, Inc.Systems and methods for processing sensor data
US12245781B2 (en)2007-12-202025-03-11Angiodynamics, Inc.Systems and methods for removing undesirable material within a circulatory system
US12318097B2 (en)2007-12-202025-06-03Angiodynamics, Inc.Systems and methods for removing undesirable material within a circulatory system
US9192700B2 (en)2008-01-082015-11-24Bluesky Medical Group, Inc.Sustained variable negative pressure wound treatment and method of controlling same
US20090175762A1 (en)*2008-01-082009-07-09Terumo Kabushiki KaishaOxygenator unit and oxygenator apparatus
US9999711B2 (en)2008-01-082018-06-19Bluesky Medical Group Inc.Sustained variable negative pressure wound treatment and method of controlling same
US11395872B2 (en)2008-01-082022-07-26Smith & Nephew, Inc.Sustained variable negative pressure wound treatment and method of controlling same
US20100298792A1 (en)*2008-01-082010-11-25Bluesky Medical Group Inc.Sustained variable negative pressure wound treatment and method of controlling same
US11116885B2 (en)2008-01-082021-09-14Smith & Nephew, Inc.Sustained variable negative pressure wound treatment and method of controlling same
US10493182B2 (en)2008-01-082019-12-03Smith & Nephew, Inc.Sustained variable negative pressure wound treatment and method of controlling same
US8366692B2 (en)2008-01-082013-02-05Richard Scott WestonSustained variable negative pressure wound treatment and method of controlling same
US11058807B2 (en)2008-03-122021-07-13Smith & Nephew, Inc.Negative pressure dressing and method of using same
US11744741B2 (en)2008-03-122023-09-05Smith & Nephew, Inc.Negative pressure dressing and method of using same
US10602968B2 (en)2008-03-252020-03-31Dexcom, Inc.Analyte sensor
US8396528B2 (en)2008-03-252013-03-12Dexcom, Inc.Analyte sensor
US11896374B2 (en)2008-03-252024-02-13Dexcom, Inc.Analyte sensor
US8834452B2 (en)2008-05-212014-09-16Smith & Nephew, Inc.Wound therapy system and related methods therefor
US20090292263A1 (en)*2008-05-212009-11-26Tyco Healthcare Group, LpWound therapy system with portable container apparatus
US9974890B2 (en)2008-05-212018-05-22Smith & Nephew, Inc.Wound therapy system and related methods therefor
US10967106B2 (en)2008-05-212021-04-06Smith & Nephew, Inc.Wound therapy system and related methods therefor
US8414519B2 (en)2008-05-212013-04-09Covidien LpWound therapy system with portable container apparatus
US9375521B2 (en)2008-05-212016-06-28Smith & Nephew, Inc.Wound therapy system and related methods therefor
US10912869B2 (en)2008-05-212021-02-09Smith & Nephew, Inc.Wound therapy system with related methods therefor
US8696626B2 (en)*2008-07-302014-04-15Claudia F. E. KirschDebubbler
EP2318064A4 (en)*2008-07-302014-06-04Claudia F E KirschDebubbler
US20100030151A1 (en)*2008-07-302010-02-04Claudia KirschDebubbler
US20100042059A1 (en)*2008-08-082010-02-18Benjamin Andrew PrattReduced-pressure treatment systems with reservoir control
US8366691B2 (en)2008-08-082013-02-05Kci Licensing, IncReduced-pressure treatment systems with reservoir control
US20100133175A1 (en)*2008-10-202010-06-03Photonic Biosystems, Inc.Filtered Assay Device and Method
WO2010047781A3 (en)*2008-10-202010-08-26Photonic Biosystems, Inc.Filtered assay device and method
US8968681B2 (en)2008-10-202015-03-03Photonic Biosystems Inc.Filtered assay device and method
US10980461B2 (en)2008-11-072021-04-20Dexcom, Inc.Advanced analyte sensor calibration and error detection
US10111991B2 (en)2009-04-172018-10-30Smith & Nephew, Inc.Negative pressure wound therapy device
US8663198B2 (en)2009-04-172014-03-04Kalypto Medical, Inc.Negative pressure wound therapy device
US9579431B2 (en)2009-04-172017-02-28Kalypto Medical, Inc.Negative pressure wound therapy device
CN102405070B (en)*2009-04-232016-01-20费森尼斯医疗德国公司For the treatment of the device of medical fluid, external functional device and treatment facility
AU2010238834B2 (en)*2009-04-232015-06-18Fresenius Medical Care Deutschland GmbhDevice, external functional device and treatment device for treating medical fluids
US20100270222A1 (en)*2009-04-232010-10-28Fresenius Medical Care Deutschland GmbhDevice and external functional means and treatment apparatus for the treatment of medical fluids
US9999736B2 (en)*2009-04-232018-06-19Fresenius Medical Care Deutschland GmbhDevice and external functional means and treatment apparatus for the treatment of medical fluids
CN102405070A (en)*2009-04-232012-04-04费森尼斯医疗德国公司Device for treating a medical fluid, external functional device and treatment apparatus
US11229729B2 (en)2009-05-292022-01-25Livanova Deutschland GmbhDevice for establishing the venous inflow to a blood reservoir of an extracorporeal blood circulation system
US11844892B2 (en)2009-05-292023-12-19Livanova Deutschland GmbhDevice for establishing the venous inflow to a blood reservoir of an extracorporeal blood circulation system
US20120130299A1 (en)*2009-05-292012-05-24Sorin Group Deutschland GmbhDevice for Establishing the Venous Inflow to a Blood Reservoir of an Extracorporeal Blood Circulation System
US9452250B2 (en)2009-06-252016-09-27Sorin Group Deutschland GmbhDevice for pumping blood in an extracorporeal circuit
US20110068061A1 (en)*2009-09-222011-03-24Haemonetics CorporationIntegrated Measurement System For Use with Surgical Fluid Salvage Containers
US8157103B2 (en)2009-09-222012-04-17Haemonetics CorporationReservoir for use with a blood collection system
US8628671B2 (en)2009-09-222014-01-14Haemonetics CorporationMethod for pre-filtering blood in a blood collection and processing system
US8512566B2 (en)*2009-12-112013-08-20General Electric CompanyDisposable fluid path systems and methods for processing complex biological materials
CN102639167A (en)*2009-12-112012-08-15通用电气公司Disposable fluid path systems and methods for processing complex biological materials
US20110139723A1 (en)*2009-12-112011-06-16General Electric CompanyDisposable fluid path systems and methods for processing complex biological materials
CN102639167B (en)*2009-12-112015-08-19通用电气公司Disposable fluid path systems and methods for processing complex biological materials
US9061095B2 (en)2010-04-272015-06-23Smith & Nephew PlcWound dressing and method of use
US12414878B2 (en)2010-04-272025-09-16Smith & Nephew PlcWound dressing and method of use
US9808561B2 (en)2010-04-272017-11-07Smith & Nephew PlcWound dressing and method of use
US10159604B2 (en)2010-04-272018-12-25Smith & Nephew PlcWound dressing and method of use
US11090195B2 (en)2010-04-272021-08-17Smith & Nephew PlcWound dressing and method of use
US12419789B2 (en)2010-04-272025-09-23Smith & Nephew PlcWound dressing and method of use
US12414877B2 (en)2010-04-272025-09-16Smith & Nephew PlcWound dressing and method of use
US11058587B2 (en)2010-04-272021-07-13Smith & Nephew PlcWound dressing and method of use
US12419788B2 (en)2010-04-272025-09-23Smith & Nephew PlcWound dressing and method of use
US8173018B2 (en)2010-08-252012-05-08Dow Global Technologies LlcFluid filter module including sealed boss
US8261919B2 (en)2010-08-252012-09-11Dow Global Technologies LlcFluid filter module including handle
US10081788B2 (en)2010-08-252018-09-25Repligen CorporationDevice, system and process for modification or concentration of cell-depleted fluid
US9446354B2 (en)2010-08-252016-09-20Repligen CorporationDevice, system and process for modification or concentration of cell-depleted fluid
US11225637B2 (en)2010-08-252022-01-18Repligen CorporationEnclosed filtration system processes
US20120271254A1 (en)*2011-02-222012-10-25Schafer Mark ECanister for autologous fat transfer
US8858518B2 (en)*2011-02-222014-10-14Mark E. SchaferCanister for autologous fat transfer
US20130092630A1 (en)*2011-03-112013-04-18Fenwal, Inc.Disposable Fluid Circuits And Methods For Cell Washing With On-Line Dilution Of Cell Feed
US9744498B2 (en)*2011-03-112017-08-29Fenwal, Inc.Disposable fluid circuits and methods for cell washing with on-line dilution of cell feed
US12245788B2 (en)2011-03-152025-03-11Angiodynamics, Inc.Device and method for removing material from a hollow anatomical structure
US12178467B2 (en)2011-03-152024-12-31Angiodynamics, Inc.Device and method for removing material from a hollow anatomical structure
US8945074B2 (en)2011-05-242015-02-03Kalypto Medical, Inc.Device with controller and pump modules for providing negative pressure for wound therapy
US9058634B2 (en)2011-05-242015-06-16Kalypto Medical, Inc.Method for providing a negative pressure wound therapy pump device
US10300178B2 (en)2011-05-262019-05-28Smith & Nephew, Inc.Method for providing negative pressure to a negative pressure wound therapy bandage
US12097095B2 (en)2011-05-262024-09-24Smith & Nephew, Inc.Method and apparatus for providing negative pressure to a negative pressure wound therapy bandage
US9067003B2 (en)2011-05-262015-06-30Kalypto Medical, Inc.Method for providing negative pressure to a negative pressure wound therapy bandage
US10213541B2 (en)2011-07-122019-02-26Sorin Group Italia S.R.L.Dual chamber blood reservoir
US11389580B2 (en)2011-07-122022-07-19Sorin Group Italia S.R.L.Dual chamber blood reservoir
US12415024B2 (en)2011-07-122025-09-16Sorin Group Italia S.R.L.Dual chamber blood reservoir
US11903798B2 (en)2012-03-122024-02-20Smith & Nephew PlcReduced pressure apparatus and methods
US12186163B2 (en)2012-03-122025-01-07Smith & Nephew PlcReduced pressure apparatus and methods
US10046096B2 (en)2012-03-122018-08-14Smith & Nephew PlcReduced pressure apparatus and methods
US11129931B2 (en)2012-03-122021-09-28Smith & Nephew PlcReduced pressure apparatus and methods
US10660994B2 (en)2012-03-122020-05-26Smith & Nephew PlcReduced pressure apparatus and methods
US10549018B2 (en)2012-05-302020-02-04Lifecell CorporationDevice for harvesting, processing and transferring adipose tissue
US10300183B2 (en)*2012-05-302019-05-28Lifecell CorporationDevice for harvesting, processing and transferring adipose tissue
CN104780954A (en)*2012-08-152015-07-15旋风医疗科技股份有限公司Systems and methods for salvaging red blood cells for autotransfusion
US8986238B2 (en)*2012-08-152015-03-24Cyclone Medtech, Inc.Systems and methods for salvaging red blood cells for autotransfusion
CN104780954B (en)*2012-08-152017-05-03旋风医疗科技股份有限公司Systems and methods for salvaging red blood cells for autotransfusion
US20140050615A1 (en)*2012-08-152014-02-20Cyclone Medtech, Inc.Systems and methods for salvaging red blood cells for autotransfusion
US10076595B2 (en)2012-08-152018-09-18Cyclone Medtech, Inc.Systems and methods for blood recovery from absorbent surgical materials
US9289546B2 (en)2012-08-162016-03-22Dirk Jerome EricksonExsanguination preventing device
US9457177B2 (en)*2012-08-292016-10-04Euromi S.A.Apparatus for extracting and re-injecting adipose tissue
US20150209565A1 (en)*2012-08-292015-07-30Euromi, S.AApparatus for extracting and re-injecting adipose tissue
US9452253B2 (en)*2013-03-132016-09-27Keith SamolykCPB system with fluid volume control
US9327066B2 (en)2013-03-132016-05-03Keith SamolykCPB system with dual function blood reservoir
USRE49881E1 (en)2013-03-282024-03-26Quanta Fluid Solutions Ltd.Re-use of a hemodialysis cartridge
US10010658B2 (en)2013-05-102018-07-03Smith & Nephew PlcFluidic connector for irrigation and aspiration of wounds
US11439741B2 (en)2013-05-102022-09-13Smith & Nephew PlcFluidic connector for irrigation and aspiration of wounds
US10533151B2 (en)2013-07-232020-01-14Kaneka CorporationMethod for producing cell concentrate, and cell suspension treatment system
US10113144B2 (en)2013-07-232018-10-30Kaneka CorporationMethod for producing cell concentrate, and cell suspension treatment system
CN105408467A (en)*2013-07-232016-03-16株式会社钟化Method for producing cell concentrate, and cell suspension treatment system
US9452021B2 (en)2013-08-022016-09-27All Cell Recovery LLCSystems, methods, and apparatus for resuspending cells from surgical laundry
US10159980B2 (en)2013-08-022018-12-25All Cell Recovery LLCSystems and methods for recovering blood cells, in a controlled environment, for storage
US8945376B1 (en)2013-08-022015-02-03All Cell Recovery LLCSystems, methods, and apparatus for resuspending cells in solution
USRE50004E1 (en)2013-08-142024-06-11Quanta Dialysis Technologies Ltd.Dual haemodialysis and haemodiafiltration blood treatment device
CN103405820A (en)*2013-08-262013-11-27佛山市博新生物科技有限公司Special line for blood perfusion hemodiasysis treatment and operation method thereof
US11738128B2 (en)2013-09-242023-08-29Keith GipsonSystem and method for cardiopulmonary bypass using hypobaric oxygenation
US10668203B2 (en)2013-09-242020-06-02Keith GipsonSystem and method for cardiopulmonary bypass using hypobaric oxygenation
US10335531B2 (en)2013-09-242019-07-02Keith GipsonSystem and method for cardiopulmonary bypass using hypobaric oxygenation
US12029841B2 (en)2013-09-242024-07-09Keith GipsonSystem and method for cardiopulmonary bypass using hypobaric oxygenation
US20160375185A1 (en)*2014-02-242016-12-29Fresenius Kabi Deutschland GmbhApparatus and method for determining the liquid level of salvaged blood in a blood collection reservoir of an autologous blood transfusion system
US10111992B2 (en)*2014-02-242018-10-30Fresenius Kabi Deutschland GmbhApparatus and method for determining the liquid level of salvaged blood in a blood collection reservoir of an autologous blood transfusion system
US10458833B2 (en)2014-05-162019-10-29Sorin Group Italia S.R.L.Blood reservoir with fluid volume measurement based on pressure sensor
US12161787B2 (en)2014-06-022024-12-10Quanta Dialysis Technologies LimitedMethod of heat sanitization of a haemodialysis water circuit using a calculated dose
US11583618B2 (en)2014-06-022023-02-21Quanta Dialysis Technologies LimitedMethod of heat sanitization of a haemodialysis water circuit using a calculated dose
CN104096275A (en)*2014-07-182014-10-15杨国锋Post-operation auto-blood recycling device
US20170246376A1 (en)*2014-10-072017-08-31Haemonetics CorporationSystem and Method for Washing Shed Blood
US10500330B2 (en)*2014-10-072019-12-10Haemonetics CorporationSystem and method for washing shed blood
WO2016057664A1 (en)2014-10-072016-04-14Haemonetics CorporationSystem and method for washing shed blood
EP3204062A4 (en)*2014-10-072018-05-16Haemonetics CorporationSystem and method for washing shed blood
US12059325B2 (en)2015-04-272024-08-13Smith & Nephew PlcReduced pressure apparatuses and methods
US10898388B2 (en)2015-04-272021-01-26Smith & Nephew PlcReduced pressure apparatuses and methods
US11571499B2 (en)2015-12-302023-02-07Quanta Dialysis Technologies Ltd.Dialysis machine
US12163513B2 (en)2016-02-102024-12-10Quanta Dialysis Technologies Ltd.Membrane pump usage condition detection
CN105536086A (en)*2016-02-232016-05-04南京医科大学第一附属医院Multifunctional ECMO circulating pipeline and method for performing extracorporeal membrane oxygenation by utilizing multifunctional ECMO circulating pipeline
US12396895B2 (en)2016-03-072025-08-26Smith & Nephew PlcWound treatment apparatuses and methods with negative pressure source integrated into wound dressing
US11723809B2 (en)2016-03-072023-08-15Smith & Nephew PlcWound treatment apparatuses and methods with negative pressure source integrated into wound dressing
US11285047B2 (en)2016-04-262022-03-29Smith & Nephew PlcWound dressings and methods of use with integrated negative pressure source having a fluid ingress inhibition component
US12121420B2 (en)2016-04-262024-10-22Smith & Nephew PlcWound dressings and methods of use with integrated negative pressure source having a fluid ingress inhibition component
US12268577B2 (en)2016-05-032025-04-08Smith & Nephew PlcOptimizing power transfer to negative pressure sources in negative pressure therapy systems
US11305047B2 (en)2016-05-032022-04-19Smith & Nephew PlcSystems and methods for driving negative pressure sources in negative pressure therapy systems
US11896465B2 (en)2016-05-032024-02-13Smith & Nephew PlcNegative pressure wound therapy device activation and control
US11096831B2 (en)2016-05-032021-08-24Smith & Nephew PlcNegative pressure wound therapy device activation and control
US11173240B2 (en)2016-05-032021-11-16Smith & Nephew PlcOptimizing power transfer to negative pressure sources in negative pressure therapy systems
US11541161B2 (en)2016-06-242023-01-03Haemonetics CorporationSystem and method for continuous flow red blood cell washing
US11116669B2 (en)2016-08-252021-09-14Smith & Nephew PlcAbsorbent negative pressure wound therapy dressing
US11648152B2 (en)2016-08-252023-05-16Smith & Nephew PlcAbsorbent negative pressure wound therapy dressing
US11717602B2 (en)2016-08-302023-08-08Lifecell CorporationSystems and methods for medical device control
US12127919B2 (en)2016-09-302024-10-29Smith & Nephew PlcNegative pressure wound treatment apparatuses and methods with integrated electronics
US11564847B2 (en)2016-09-302023-01-31Smith & Nephew PlcNegative pressure wound treatment apparatuses and methods with integrated electronics
US11148109B2 (en)*2016-11-162021-10-19Zyno Medical, LlcIsolatable automatic drug compounding system
US11135343B2 (en)*2016-12-012021-10-05Fenwal, Inc.Blood component pooling device, system and method
US12005181B2 (en)2016-12-122024-06-11Smith & Nephew PlcPressure wound therapy status indication via external device
US11660382B2 (en)2016-12-232023-05-30Quanta Dialysis Technologies LimitedValve leak detection system
US12011528B2 (en)2017-02-022024-06-18Quanta Dialysis Technologies Ltd.Phased convective operation
US11365728B2 (en)2017-02-242022-06-21Quanta Dialysis Technologies Ltd.Testing rotor engagement of a rotary peristaltic pump
US11123471B2 (en)2017-03-082021-09-21Smith & Nephew PlcNegative pressure wound therapy device control in presence of fault condition
US11160915B2 (en)2017-05-092021-11-02Smith & Nephew PlcRedundant controls for negative pressure wound therapy systems
CN110913921A (en)*2017-05-122020-03-24斯特拉斯克莱德大学Limb stabilization device and method
WO2018206941A1 (en)*2017-05-122018-11-15University Of StrathclydeLimb stabilisation apparatus and methods
US12251504B2 (en)*2017-06-302025-03-18Quanta Dialysis Technologies Ltd.Dialysis systems, devices and methods
US12097097B2 (en)2017-09-132024-09-24Smith & Nephew PlcNegative pressure wound treatment apparatuses and methods with integrated electronics
US11701265B2 (en)2017-09-132023-07-18Smith & Nephew PlcNegative pressure wound treatment apparatuses and methods with integrated electronics
US11564845B2 (en)2017-09-132023-01-31Smith & Nephew PlcNegative pressure wound treatment apparatuses and methods with integrated electronics
USD1070090S1 (en)2017-09-282025-04-08Quanta Dialysis Technologies Ltd.Dialysis machine
US11350862B2 (en)2017-10-242022-06-07Dexcom, Inc.Pre-connected analyte sensors
US12150250B2 (en)2017-10-242024-11-19Dexcom, Inc.Pre-connected analyte sensors
US11382540B2 (en)2017-10-242022-07-12Dexcom, Inc.Pre-connected analyte sensors
US11706876B2 (en)2017-10-242023-07-18Dexcom, Inc.Pre-connected analyte sensors
US11943876B2 (en)2017-10-242024-03-26Dexcom, Inc.Pre-connected analyte sensors
US11331022B2 (en)2017-10-242022-05-17Dexcom, Inc.Pre-connected analyte sensors
US12128170B2 (en)2017-11-012024-10-29Smith & Nephew PlcNegative pressure wound treatment apparatuses and methods with integrated electronics
US11554203B2 (en)2017-11-012023-01-17Smith & Nephew PlcNegative pressure wound treatment apparatuses and methods with integrated electronics
US12324729B2 (en)2017-11-012025-06-10Smith & Nephew PlcNegative pressure wound treatment apparatuses and methods with integrated electronics
US11992392B2 (en)2017-11-012024-05-28Smith & Nephew PlcNegative pressure wound treatment apparatuses and methods with integrated electronics
US11497653B2 (en)2017-11-012022-11-15Smith & Nephew PlcNegative pressure wound treatment apparatuses and methods with integrated electronics
US11707564B2 (en)2017-11-012023-07-25Smith & Nephew PlcSafe operation of integrated negative pressure wound treatment apparatuses
USD898925S1 (en)2018-09-132020-10-13Smith & Nephew PlcMedical dressing
USD999914S1 (en)2018-09-132023-09-26Smith & Nephew PlcMedical dressing
US20210268163A1 (en)*2018-11-272021-09-02Terumo Kabushiki KaishaOxygenator
US11986583B2 (en)*2018-11-272024-05-21Terumo Kabushiki KaishaOxygenator
US11850047B2 (en)*2019-01-182023-12-26Becton, Dickinson And CompanyBlood collection system including a baffle
US11439333B2 (en)*2019-01-182022-09-13Becton, Dickinson And CompanyBlood collection system including a baffle
US20220369969A1 (en)*2019-01-182022-11-24Becton, Dickinson And CompanyBlood collection system including a baffle
US12083263B2 (en)2019-03-202024-09-10Smith & Nephew PlcNegative pressure wound treatment apparatuses and methods with integrated electronics
US12005182B2 (en)2019-05-312024-06-11T.J.Smith And Nephew, LimitedSystems and methods for extending operational time of negative pressure wound treatment apparatuses
US12357738B2 (en)2019-05-312025-07-15Quanta Dialysis Technologies LimitedSource container connector
US12311091B2 (en)*2019-06-272025-05-27Livanova Deutschland GmbhDevice for automatically establishing the venous inflow to a blood reservoir of an extracorporeal blood circulation system
US20220080094A1 (en)*2019-06-272022-03-17Livanova Deutschland GmbhDevice for Automatically Establishing the Venous Inflow to a Blood Reservoir of an Extracorporeal Blood Circulation System
US11266825B2 (en)*2020-02-202022-03-08First Pass, LlcManual clot aspiration and filtration system and method of removing a clot
US12311093B2 (en)2020-02-202025-05-27First Pass, LlcManual clot aspiration and filtration system and method of removing a clot
CN115475288A (en)*2021-05-312022-12-16深圳麦科田生命科学有限公司Suction device and suction method
US20240173042A1 (en)*2021-10-182024-05-30Imperative Care, Inc.Device for clot retrieval with varying tube diameters
CN114470384A (en)*2022-02-172022-05-13四川大学华西医院Negative pressure type extracorporeal circulation blood suction system
US20240033408A1 (en)*2022-07-282024-02-01Cardiacassist, Inc.Extracorporeal life support system with blood recirculation pathway
CN119098054A (en)*2024-09-052024-12-10洁翼流体技术(上海)有限公司 A ceramic membrane microfiltration device for separating milk whey protein
CN119098054B (en)*2024-09-052025-09-09洁翼流体技术(上海)有限公司Ceramic membrane microfiltration equipment for separating milk whey protein

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EP0518975B1 (en)1997-05-02
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EP0518975A4 (en)1993-01-20
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JP3012689B2 (en)2000-02-28
DE69125931D1 (en)1997-06-05

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